A new approach for scale-up of bubble column reactors

被引:19
|
作者
Youssef, Ahmed A. [1 ]
Hamed, Mohamed E. [2 ]
Al-Dahhan, Muthanna H. [3 ]
Dudukovic, Milorad P. [4 ]
机构
[1] SABIC, Mt Vernon, IN 47620 USA
[2] Sasol, Enschede, Netherlands
[3] Missouri Univ Sci & Technol MST, Chem & Biol Engn Dept, Rolla, MO 65409 USA
[4] Washington Univ, CREL, Energy Environm & Chem Engn Dept, St Louis, MO 63130 USA
来源
关键词
Bubble columns; Internals; Hydrodynamics; Scale-up; Compartmentalization; SLURRY REACTOR; DESIGN; SIMILITUDE; STRATEGY;
D O I
10.1016/j.cherd.2013.12.011
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The reactor of choice for the Fischer-Tropsch synthesis is a slurry bubble column. One of the few disadvantages of bubble columns is the difficulties associated with their scale-up. The latter is due to complex phases' interactions and significant back-mixing. For a proper scaling dimensionless numbers should be kept constant in the various scales in order to ensure both dynamic and geometrical similarity. With the complex nature of the flow in these systems, this becomes very hard to achieve. Hence, innovative approaches to provide a firm scale-up methodology are needed. Controlling the effect of scale using heat exchanging internals by means of reactor compartmentalization is proposed in this study. Preliminary results show that radial gas holdup profiles as well as other bubble dynamics inside the compartments exhibited similar behavior as inside a solid wall column, since the comparison between the single tube bundle compartment and data obtained in 6 inches steel bubble column shows good match. (C) 2013 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:1637 / 1646
页数:10
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