Direct numerical simulation of a non-isothermal non-adiabatic packed bed reactor

被引:30
作者
Chandra, V [1 ]
Peters, E. A. J. F. [1 ]
Kuipers, J. A. M. [1 ]
机构
[1] Eindhoven Univ Technol, Dept Chem Engn & Chem, Multiphase Reactors Grp, POB 513, NL-5600 MB Eindhoven, Netherlands
关键词
Direct numerical simulation; Packed bed reactors; Immersed Boundary Method; Hot-spot; Heat and mass transfer; MULTIPLE STEADY-STATES; HEAT-TRANSFER; MASS-TRANSFER; DYNAMIC-BEHAVIOR; CFD SIMULATIONS; FLOW; TRANSPORT; FLUID; WALL; DISPERSION;
D O I
10.1016/j.cej.2019.123641
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A fundamental continuum-based numerical model was developed to simulate a non-isothermal non-adiabatic reactor which does not employ any empirical closures. The model was able to capture unique features of an exothermic catalytic reactor such as parametric sensitivity, hot-spot formations and multiplicity of steady states. Furthermore, the model inherently accounts for the various aspects of classical phenomenological models such as axial and radial dispersion of heat and mass and the intrinsic coupling of heat and mass transport between the fluid phase and the solid phase. The numerical procedure was validated with existing literature data before moving on to the simulation of a bed consisting of 340 spherical particles packed using the Discrete Element Method. Five simulations were performed by varying the rate of reaction and keeping all other parameters constant to capture the ignition/extinction phenomena exhibited by exothermic packed bed reactors.
引用
收藏
页数:16
相关论文
共 56 条
[41]  
Shah R.K., 2014, Laminar Flow Forced Convection in ducts: a Source Book for Compact Heat Exchanger Analytical Data
[42]   Coupling the fictitious domain and sharp interface methods for the simulation of convective mass transfer around reactive particles: Towards a reactive Sherwood number correlation for dilute systems [J].
Sulaiman, Mostafa ;
Hammouti, Abdelkader ;
Climent, Eric ;
Wachs, Anthony .
CHEMICAL ENGINEERING SCIENCE, 2019, 198 :334-351
[43]   Pseudo-turbulent heat flux and average gas-phase conduction during gas-solid heat transfer: flow past random fixed particle assemblies [J].
Sun, Bo ;
Tenneti, Sudheer ;
Subramaniam, Shankar ;
Koch, Donald L. .
JOURNAL OF FLUID MECHANICS, 2016, 798 :299-349
[44]   A New Drag Correlation from Fully Resolved Simulations of Flow Past Monodisperse Static Arrays of Spheres [J].
Tang, Y. ;
Peters, E. A. J. F. ;
Kuipers, J. A. M. ;
Kriebitzsch, S. H. L. ;
van der Hoef, M. A. .
AICHE JOURNAL, 2015, 61 (02) :688-698
[45]   Direct numerical simulation of particulate flow with heat transfer [J].
Tavassoli, H. ;
Kriebitzsch, S. H. L. ;
van der Hoef, M. A. ;
Peters, E. A. J. F. ;
Kuipers, J. A. M. .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2013, 57 :29-37
[46]   Relation between catalytic activity and size of particle [J].
Thiele, EW .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1939, 31 :916-920
[47]   THE CHARACTER OF THE STATIONARY STATE OF EXOTHERMIC PROCESSES [J].
VANHEERDEN, C .
CHEMICAL ENGINEERING SCIENCE, 1958, 8 (1-2) :133-145
[48]   DISCRIMINATION OF 3 APPROACHES TO EVALUATE HEAT FLUXES FOR WALL-COOLED FIXED-BED CHEMICAL REACTORS [J].
VORTMEYER, D ;
HAIDEGGER, E .
CHEMICAL ENGINEERING SCIENCE, 1991, 46 (10) :2651-2660
[49]   EVALUATION OF STEADY FLOW PROFILES IN RECTANGULAR AND CIRCULAR PACKED-BEDS BY A VARIATIONAL METHOD [J].
VORTMEYER, D ;
SCHUSTER, J .
CHEMICAL ENGINEERING SCIENCE, 1983, 38 (10) :1691-1699
[50]   MOVING REACTION ZONES IN FIXED BED REACTORS UNDER INFLUENCE OF VARIOUS PARAMETERS [J].
VORTMEYER, D ;
JAHNEL, W .
CHEMICAL ENGINEERING SCIENCE, 1972, 27 (08) :1485-+