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A Mass Transfer Model Based on Individual Bubbles and an Unsteady State Film Mechanism 被引量:1

A Mass Transfer Model Based on Individual Bubbles and an Unsteady State Film Mechanism
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摘要 A gas-liquid mass transfer model based on an unsteady state film mechanism applied to a single bubble is presented. The mathematical model was solved using Laplace transform to obtain an analytical solution of concentration profile in terms of the radial position r and time t. The dynamic mass transfer flux was deduced and the influence of the bubble size was also determined. A mathematical method for deducing the average mass transfer flux directly from the Laplace transformed concentration is presented. Its accuracy is verified by comparing the numerical results with those from the indirect method. The influences of the model parameters, namely, the bubble size R, liquid film thickness δ, and the surface renewal constant s on the average mass transfer flux were investigated. The proposed model is useful for a better understanding of the mass transfer mechanism and an optimum design of gas-liquid contact equipment. A gas-liquid mass transfer model based on an unsteady state film mechanism applied to a single bubble is presented. The mathematical model was solved using Laplace transform to obtain an analytical solution of concentration profile in terms of the radial position r and time t. The dynamic mass transfer flux was deduced and the influence of the bubble size was also determined. A mathematical method for deducing the average mass transfer flux directly from the Laplace transformed concentration is presented. Its accuracy is verified by comparing the numerical results with those from the indirect method. The influences of the model parameters, namely, the bubble size R, liquid film thickness δ, and the surface renewal constant s on the average mass transfer flux were investigated. The proposed model is useful for a better understanding of the mass transfer mechanism and an optimum design of gas-liquid contact equipment.
出处 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2004年第2期163-168,共6页 中国化学工程学报(英文版)
基金 Supported by the National Science Foundation of China (No. 20276035) and the SINOPEC Fundamental Research Foundation (No.X500021).
关键词 薄膜理论 气体 液体 转移模式 表面恢复理论 渗透理论 扩散 film theory, Laplace transformation, mass diffusion, penetration theory, surface renewal theory
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  • 1刘永民,刘铮,袁乃驹.多管环流反应器的流动和传质特性[J].化工学报,2001,52(3):222-226. 被引量:28
  • 2Calderbank, P.H.,Johnson, D.S.L.,Loudon, J."Mechan-ics and mass transfer of single bubbles in free rise through some Newtonian and non-Newtonian liquids"[].Chemical Engineering Science.1970
  • 3Koide, K.,Hayashi, T.,Sumino, K.,Iwamoto, S."Mass transfer from single bubbles in aqueous solutions of surfac-tants"[].Chemical Engineering Science.1976
  • 4Koide, K.,Orito, Y.,Hara, Y."Mass transfer from single bubbles in Newtonian liquids"[].Chemical Engineering Science.1974
  • 5Bird, R.B.,Stewart, W.B.,Lightfoot, E.N.Transport Phe-nomena[]..2002
  • 6Toor,H.L.,Marchello,J.M.Film-Penetration Model for Mass and Heat Transfer[].American Institute of Chemical Engineers Journal.1958
  • 7.
  • 8Whitman WG.Preliminary experimental confirmation of the two-film theory of gas adsorption[].Chemistry Metal Engineering.1923
  • 9Higbie R.The rate of adsorption of a pure gas into a still liquid during short periods of exposure[].Transactions of the American Institute of Chemical Engineers.1935
  • 10Danckwerts P V.Significance of liquid-film coefficients in gas absorption[].Industrial and Engineering Chemistry.1951

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