Comparison of hydrodynamic parameters for countercurrent and cocurrent flow through packed beds

被引:28
作者
Iliuta, I
Thyrion, FC
Bolle, L
Giot, M
机构
[1] UNIV CATHOLIQUE LOUVAIN,INST CHEM ENGN,B-1348 LOUVAIN,BELGIUM
[2] UNIV CATHOLIQUE LOUVAIN,LAB THERMODYNAM,B-1348 LOUVAIN,BELGIUM
关键词
D O I
10.1002/ceat.270200304
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Hydrodynamic parameters have been determined in common equipment, i.e., same column and liquid and gas distributors, for cocurrent and countercurrent two-phase flow through fixed beds. The piston/dispersion exchange model (PDE) with usual Danckwerts' boundary conditions (closed/closed system) has been used to describe the liquid flow. A new imperfect pulse method has been used to estimate the PDE model parameters directly from the experimentally nonideal input and output response. The transition between trickle flow and pulse flow, for two-phase downflow, and the occurrence of flooding, for countercurrent flow, has been investigated using a macroscopic model for the two-phase flow.
引用
收藏
页码:171 / 181
页数:11
相关论文
共 33 条
[31]   A MODEL REPRESENTING RESIDENCE-TIME DISTRIBUTION IN A SEMI-INFINITE REACTOR WITH AXIAL DISPERSION AND STAGNANT ZONES . APPLICATION TO TRICKLE FLOW IN COLUMNS WITH RASCHIG RINGS [J].
VILLERMAUX, J ;
VANSWAAI.WP .
CHEMICAL ENGINEERING SCIENCE, 1969, 24 (07) :1097-+
[32]   RESIDENCE TIME DISTRIBUTION OF THE LIQUID IN GAS-LIQUID COCURRENT UPFLOW FIXED-BED REACTORS WITH POROUS PARTICLES [J].
YANG, XL ;
EUZEN, JP ;
WILD, G .
CHEMICAL ENGINEERING SCIENCE, 1990, 45 (11) :3311-3317
[33]  
Zhukova TB, 1990, INT CHEM ENG, V30, P57