Hydrodynamics and mass transfer in an airlift reactor

被引:49
作者
Korpijarvi, J
Oinas, P
Reunanen, J
机构
[1] Kemira Fine Chem Oy, Kokkola 67101, Finland
[2] Tampere Univ Technol, Tampere 30101, Finland
[3] Kemira Chem Oy, Oulu 90101, Finland
关键词
airlift; reactor; hydrodynamics; mass transfer; axial dispersion; gas hold-up;
D O I
10.1016/S0009-2509(98)00439-4
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Hydrodynamics and mass transfer in internal and external flow airlift reactors have been studied in this work, Gas hold-ups and liquid velocities have been determined in a concentric tube airlift reactor, while oxygen mass transfer has been measured in an external loop airlift reactor. First, tracer measurements were used to verify a conventional axial dispersion model. Further, a model derived from multi-phase Navier-Stokes equations was verified with experimental data from the oxygen mass transfer measurements. Both models were in a good agreement with the measurements. (C) 1999 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:2255 / 2262
页数:8
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