Application of the penetration theory for gas-liquid mass transfer without liquid bulk: Differences with system with a bulk

E.P. van Elk* (Corresponding Author), M.C. Knaap, G.F. Versteeg

*Corresponding author for this work

Research output: Contribution to journalArticleAcademicpeer-review

19 Citations (Scopus)

Abstract

Frequently applied micro models for gas-liquid mass transfer all assume the presence of a liquid bulk. However, some systems are characterized by the absence of a liquid bulk, a very thin layer of liquid flows over a solid surface. An example of such a process is absorption in a column equipped with sructured packing elements. The penetration model was slightly modified, so that it can describe systems without liquid bulk. A comparison is made between the results obtained with the modified model and the results that would be obtained when applying the original penetration theory for systems with liquid bulk. Both physical absorption and absorption accompanied by first and second order chemical reaction have been investigated. It is concluded that the original penetration theory can be applied for systems without liquid bulk, provided that the liquid layer has sufficient thickness (δ > d*pen). For packed columns this means, in terms of Sherwood number, Sh ≥ 4. In case of a 1,1-reaction with Ha > 0.2 an additional second criterion is Sh ≥4√Db/Da For very thin liquid layers (Sh < 4 or Sh < 4√Db/Da), the original penetration model may give erroneous results, depending on the exact physical and chemical parameters, and the modified model is required.

Original languageEnglish
Pages (from-to)516-524
Number of pages9
JournalChemical Engineering Research and Design
Volume85
Issue number4
DOIs
Publication statusPublished - 21 Mar 2007
Externally publishedYes

Keywords

  • Film
  • Liquid layer
  • Mass transfer
  • Packed columns
  • Penetration theory
  • Structured packing

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