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  4. Modeling chemistry and flow in catalytic fixed-bed reactors with detailed geometry
 
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Modeling chemistry and flow in catalytic fixed-bed reactors with detailed geometry

Citation Link: https://doi.org/10.15480/882.1636
Publikationstyp
Doctoral Thesis
Date Issued
2018
Sprache
English
Author(s)
Dong, Ying  orcid-logo
Advisor
Horn, Raimund  
Referee
Heinrich, Stefan  
Title Granting Institution
Technische Universität Hamburg-Harburg
Place of Title Granting Institution
Hamburg
Examination Date
2018-05-04
Institut
Chemische Reaktionstechnik V-2  
TORE-DOI
10.15480/882.1636
TORE-URI
http://hdl.handle.net/11420/1639
In this work, three-dimensional CFD models were developed and applied to simulate catalytic fixed bed reactors with different types of packing configuration and reactions. A spatially resolved profile measurement technique was applied in this work to critically validate the simulation results, and to calibrate parameters required in the model. This work demonstrates that detailed reactor modeling and profile measurements are useful tools for achieving an in-depth understanding of the interactions between flow, heat and mass transfer and catalytic reactions in fixed bed reactors. Furthermore, with the comprehensive knowledge gained from both methods, a knowledge-based reactor optimization approach can be put forward.
Subjects
CFD-simulation
Fixed-bed reactor
Catalytic reaction
DDC Class
620: Ingenieurwissenschaften
Lizenz
http://rightsstatements.org/vocab/InC/1.0/
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