One-Dimensional Modeling and Simulation of Bubble Column Reactors

被引:6
作者
Jung, Sebastian [1 ]
Becker, Marc [2 ]
Agar, David W. [3 ]
Franke, Robert [1 ]
机构
[1] Evon Oxeno GmbH, D-45772 Marl, Germany
[2] Evon Degussa GmbH, Marl, Germany
[3] Tech Univ Dortmund, Lehrstuhl Tech Chem B, Dortmund, Germany
关键词
Bubble column; Modeling; Simulation; FISCHER-TROPSCH SYNTHESIS; HOMOGENEOUS REGIME; MASS-TRANSFER; SCALE-UP; LIQUID; GAS; PREDICTION; PRESSURE; FLOW;
D O I
10.1002/ceat.201000313
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Reactor models that feature a practical way to design bubble columns on the semi-industrial or even industrial scale have been published only rarely in the usual scientific literature. Creating a one-dimensional model in the equation-oriented simulation software ASPEN Custom Modeler (TM) (ACM), one can reach a compromise between model precision and modeling - i.e. computational power - based on correlations selected specifically for the application in question. The model quantitatively describes, with sufficient accuracy, the processes in a bubble column reactor. The paper discusses investigations for designing a pilot plant reactor for hydrogenating 2-ethylhexanal as an example of its application. Geometry and operating conditions were optimized, and the results are shown in the form of spatially resolved reaction and temperature profiles.
引用
收藏
页码:2037 / 2043
页数:7
相关论文
共 22 条
[1]  
[Anonymous], 2009, ULLMANNS ENCY IND CH, V7th
[2]   FLOW STUDIES ON A BUBBLE-COLUMN CASCADE REACTOR WITH UNIDIRECTIONAL FLOW OF GAS AND LIQUID [J].
BLASS, E ;
KOCH, KH .
CHEMIE INGENIEUR TECHNIK, 1972, 44 (15) :913-&
[3]   Detailed modelling of hydrodynamics, mass transfer and chemical reactions in a bubble column using a discrete bubble model:: Chemisorption of CO2 into NaOH solution, numerical and experimental study [J].
Darmana, D. ;
Henket, R. L. B. ;
Deen, N. G. ;
Kuipers, J. A. M. .
CHEMICAL ENGINEERING SCIENCE, 2007, 62 (09) :2556-2575
[4]  
Deckwer W.-D.:., 1985, Reaktionstechnik in Blasensaulen
[5]   BUBBLE COLUMN REACTORS [J].
GERSTENBERG, H .
CHEMIE INGENIEUR TECHNIK, 1979, 51 (03) :208-216
[6]  
Helfferich FG, 2003, KINETICS HOMOGENEOUS
[7]  
Higbie R, 1935, T AM INST CHEM ENG, V31, P365
[8]   HEAT-TRANSFER COEFFICIENT IN BUBBLE-COLUMNS [J].
HIKITA, H ;
ASAI, S ;
KIKUKAWA, H ;
ZAIKE, T ;
OHUE, M .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1981, 20 (03) :540-545
[9]   LIQUID-PHASE BACKMIXING IN BUBBLE-COLUMN REACTORS - A NEW CORRELATION [J].
KANTAK, MV ;
SHETTY, SA ;
KELKAR, BG .
CHEMICAL ENGINEERING COMMUNICATIONS, 1994, 127 :23-34
[10]   A scale-up strategy for a commercial scale bubble column slurry reactor for Fischer-Tropsch synthesis [J].
Krishna, R .
OIL & GAS SCIENCE AND TECHNOLOGY-REVUE D IFP ENERGIES NOUVELLES, 2000, 55 (04) :359-393