Effect of mixing behaviour on gas-liquid mass transfer in highly viscous, stirred non-newtonian liquids

When declaring and using process engineering data such as, for exmple, mixing times or kLa values, it is assumed that these apply to the entire reactor contents. The condition of uniform mixing, necessary for this, is generally met in the regime of turbulent flow. When highly viscous and, above all,...

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Veröffentlicht in:Chemical engineering & technology 1991-01, Vol.14 (1), p.1-10
Hauptverfasser: Henzler, Hans-Jürgen, Obernosterer, Gerd
Format: Artikel
Sprache:eng
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