Multistage high pressure mixer-settler system

被引:3
|
作者
Pietzonka, W
Trepp, C
机构
[1] Institute of Process Engineering and Cryogenics, Swiss Federal Institute of Technology, Zürich
来源
关键词
D O I
10.1016/S0921-8610(96)80104-X
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
An extraction apparatus has been developed for pressures up to 30 MPa and temperatures up to 120 degrees C, as an alternative to the counter-current column used in supercritical fluid extraction. The apparatus consists of five mixer-settler stages which are arranged in counter-current flow. Regenerative pumps are used as mixers to achieve an intense contact between the two phases and to create a large mass transfer surface area. Cyclones are used as separators to avoid back mixing. Previous work with a single stage module yielded a separation efficiency of about 96%. The achieved mass transfer surface area was 2'000 - 3'000 m(2)/m(3). The multistage apparatus is currently being tested. Results of separation efficiency and behaviour will therefore be presented at the sysmposium in October 1996.
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页码:609 / 614
页数:6
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