Helical Packing Columns for Preventing Foam Formation: Experimental and Numerical Investigations

被引:0
|
作者
Nesme, Anuhar Osorio [1 ]
Hohagen, Hans [1 ]
Topic, Nikola [1 ]
Thuennesen, Julian [1 ]
Mobarak, Mohammad [1 ]
Lyu, Wenjing [2 ]
Jahn, Alexander [2 ]
Kim, Sedong [2 ]
Delgado, Antonio [1 ,2 ]
机构
[1] Friedrich Alexander Erlangen Nuremberg Univ, Inst Fluid Mech, Cauerstr 4, D-91058 Erlangen, Germany
[2] LSTME Busan Branch, Busan 46742, South Korea
关键词
Foaming; Mass transfer; Packing columns; Pressure drop; Structured packing; STRUCTURED PACKING; CFD SIMULATION; LIQUID FLOW; PRESSURE-DROP; MASS-TRANSFER; EFFICIENCY;
D O I
10.1002/ceat.202200070
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Unwanted foaming and liquid bridging inside structured packings have a negative effect on the pressure drop during thermal separation processes. A novel helical design of a packing column for preventing foaming is presented. The effective interfacial area is calculated by numerical simulations. Different designs are analyzed by varying geometrical parameters such as helix pitch, channel opening angle, and number of channels. Different F-factor values and liquid loads are evaluated. Packings with larger helix pitch exhibited lower pressure drop and reduced effective interfacial area. Smaller channel opening angles increased the pressure drop and promoted unstable flow conditions. The novel packings show lower effective interfacial area than existing structured packings, but no foaming was observed in a wide range of operating conditions.
引用
收藏
页码:1404 / 1413
页数:10
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