Liquid Holdup in Catalyst-Containing Pockets of a Modular Catalytic Structured Packing

被引:10
作者
Behrens, Marcel [2 ]
Olujic, Zarko [1 ]
Jansens, Pieter J. [1 ]
机构
[1] Delft Univ Technol, Proc & Energy Lab, NL-2628 CA Delft, Netherlands
[2] Packaged Gases Technol COE, Air Prod, Vilvoorde, Belgium
关键词
Catalysts; Catalytic load point; Katapak-SP; Liquid holdup; Structured packings;
D O I
10.1002/ceat.200800236
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper introduces a simple, first principles-based model describing the I liquid holdup in the catalyst-containing pockets of Katapak-SP, a modular catalytic structured packing developed to allow a certain degree of flexibility with respect to the variation in reaction-to-separation requirements in a single unit. The basic requirement for the catalyst-containing pockets in this respect is to be fully filled with flowing liquid which implies that the operating holdup is bound between the static holdup of the catalyst bed as the lower end, and that corresponding to the upper limit, the so-called catalytic load point. The latter is the liquid load corresponding to the bed saturation point) indicating that excessive liquid will be retained, i.e., will remain in the separation part of the packing element and mix with the liquid leaving the catalyst-filled pockets at the bottom of the element. Detailed knowledge of the liquid holdup as well as the pattern of the trickling flow is essential because it governs the performance of the reaction part and consequently the hybrid unit as a whole. Both glass and resin (an industrial catalyst) particles were Used ill conjunction with water and a binary water-methanol mixture as working fluids. The model predictions for static holdup and the catalytic load agree well with the experiments.
引用
收藏
页码:1630 / 1637
页数:8
相关论文
共 23 条
[1]   In situ measurements of the static liquid holdup in Katapak-SP12™ packed column using X-ray tomography [J].
Aferka, Saied ;
Crine, Michel ;
Saroha, Anil K. ;
Toye, Dominique ;
Marchot, Pierre .
CHEMICAL ENGINEERING SCIENCE, 2007, 62 (21) :6076-6080
[2]  
Beek W. J., 1975, Transport Phenomena
[3]   Liquid flow behavior in catalyst-containing pockets of modular catalytic structured packing katapak SP [J].
Behrens, M. ;
Olujic, Z. ;
Jansens, P. J. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2007, 46 (12) :3884-3890
[4]   Combining reaction with distillation - Hydrodynamic and mass transfer performance of modular catalytic structured packings [J].
Behrens, M. ;
Olujic, Z. ;
Jansens, P. J. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2006, 84 (A5) :381-389
[5]  
Behrens M., 2006, THESIS DELFT U TECHN
[6]  
DEGARMO JL, 1992, CHEM ENG PROG, V88, P43
[7]   Counter-current operation of structured catalytically packed distillation columns: pressure drop, holdup and mixing [J].
Ellenberger, J ;
Krishna, R .
CHEMICAL ENGINEERING SCIENCE, 1999, 54 (10) :1339-1345
[8]   HYDRODYNAMICS AND SOLID-LIQUID CONTACTING EFFECTIVENESS IN TRICKLE-BED REACTORS [J].
GIANETTO, A ;
BALDI, G ;
SPECCHIA, V ;
SICARDI, S .
AICHE JOURNAL, 1978, 24 (06) :1087-1104
[9]   Reactive distillation with KATAPAK® [J].
Götze, L ;
Bailer, O ;
Moritz, P ;
von Scala, C .
CATALYSIS TODAY, 2001, 69 (1-4) :201-208
[10]   Reactive distillation: The front-runner of industrial process intensification - A full review of commercial applications, research, scale-up, design and operation [J].
Harmsen, G. Jan .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2007, 46 (09) :774-780