Methodology for modeling detailed imperfect mixing effects in complex reactors

被引:41
作者
Wells, GJ [1 ]
Ray, WH [1 ]
机构
[1] Univ Wisconsin, Dept Chem & Biol Engn, Madison, WI 53706 USA
关键词
mixing; compartment models; computational fluid dynamics; low-density polyethylene; autoclave reactor;
D O I
10.1002/aic.10407
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A powerful new modeling technique is presented for exploring mixing effects in reactive flow systems. The technique combines the detailed mixing representation of computational fluid dynamics (CFD) simulations with the simplicity and computational efficiency of stirred-tank compartment models. The method can be generally applied to many reactive systems, and requires only that appropriate criteria be specified to select compartment models from a single converged CFD simulation. A 1000-fold increase in computational speed is achieved by the new compartment model/CFD technique when modeling steady-state operation of low-density polyethylene (LDPE) autoclave reactors, making broad studies of operating conditions and stability possible. Results from compartment models are shown to capture the accuracy and detail of CFD simulations over a wide range of LDPE reactor operation, and the new technique provides a combination of modeling detail and computational ease not previously available for this type of reactor. (c) 2005 American Institute of Chemical Engineers.
引用
收藏
页码:1508 / 1520
页数:13
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