Download presentation
Presentation is loading. Please wait.
Published byDamaris Hutton Modified over 9 years ago
1
Master’s Dissertation Defense Carlos M. Teixeira Supervisors: Prof. José Carlos Lopes Eng. Matthieu Rolland Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing 17 th July 2013
2
2 Outline FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Introduction Objectives State of the Art Methodology Results and Discussion Conclusions
3
3 Introduction FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing
4
4 Introduction FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Reactors with low tube-to-particle diameter ratio Pseudo Homogeneous Models may not be valid Local Phenomena are dominant Wall Effect Packing Effect
5
5 Introduction FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Example of Packing Effect Problem Description Packing of eight cylinders with different arrangements Fluid with zero concentration at the inlet flows through the packing Laminar regime Cylinders with constant concentration in their surface Transfer solute to the fluid Normalized outlet concentration for the different arrangements
6
6 Outline FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Introduction Objectives State of the Art Methodology Results and Discussion Conclusions
7
7 Objectives FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Study the phenomena of single phase fluid flow through fixed-bed reactors at low particle Reynolds number Understand how the packing structure affects the flow
8
8 Outline FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Introduction Objectives State of the Art Methodology Results and Discussion Conclusions
9
9 State of the Art FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing CFD Simulation of Fixed-Bed Reactors
10
10 State of the Art FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Coupling between Hydrodynamics, Heat Transfer and Chemical Reaction: Less works on the literature Applied in small size problems (dozens of particles) Particle shape: mostly spheres CFD Simulation of Fixed-Bed Reactors
11
11 Outline FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Introduction Objectives State of the Art Methodology Results and Discussion Conclusions
12
12 Methodology FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Coupling between DEM and CFD GRAINS3D (Packing Simulation) PeliGRIFF (Fluid Flow Simulation)
13
13 Methodology FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Grid Refinement Studies Relative error in the inlet velocity as a function of the grid resolution (ε=0.799, l/d p =1)
14
14 Outline FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Introduction Objectives State of the Art Methodology Results and Discussion Conclusions
15
15 Results and Discussion FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Flow through Structured Packed Beds Unit cell approach A packed bed of simple cubic arrangement of spheres. a) Unit cell b) Alternative representation of a simple cubic unit cell. (a) (b)
16
16 Results and Discussion FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Flow through Structured Packed Beds of Spheres Validation Case Comparison between the simulated dimensionless pressure drop and results from Hill et al. (2001) for a dilute array of spheres (ε=0.799)
17
17 Results and Discussion FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Effect of cylinder orientation Effect of cylinders orientation on dimensionless pressure drop (ε=0.799, l/d p =1) Flow through Structured Packed Beds of Cylinders
18
18 Results and Discussion FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Transition from laminar regime to unsteady and chaotic flow Flow through Structured Packed Beds of Cylinders Particle Reynolds number as a function of time for 45º orientation (ΔP=10 Pa)
19
19 Results and Discussion FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Flow through Randomly Packed Beds of Cylinders Case ID FBR1 FBR2 FBR3 Nº of particles 540 200 100 Porosity, ε 0.451 0.444 0.467
20
20 Results and Discussion FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Flow through Randomly Packed Beds of Cylinders Simulated Packed Beds
21
21 Results and Discussion FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Flow through Randomly Packed Beds of Cylinders Pressure Drop Dimensionless pressure drop as a function of porosity. Comparison between simulations and Ergun correlation predictions (Re dp =1).
22
22 Results and Discussion FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Flow through Randomly Packed Beds of Cylinders Spatial Velocity Distribution Three different zones are identified: Recirculation zones in the packing top and bottom and in the wake of the particles (with negative velocities) High velocity zones where the void fraction is small and the velocity increases up to a factor of 15 Low velocity zones near the particles surfaces
23
23 Results and Discussion FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Flow through Randomly Packed Beds of Cylinders Statistical Velocity Distribution Probability density functions of normalized z-velocity in different zones of the fixed-bed.
24
24 Results and Discussion FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Flow through Randomly Packed Beds of Cylinders Statistical Velocity Distribution (link with porosity) Inlet Outlet Axial average porosity profile
25
25 Results and Discussion FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Flow through Randomly Packed Beds of Cylinders Statistical Velocity Distribution (link with porosity)
26
26 Results and Discussion FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Flow through Randomly Packed Beds of Cylinders Statistical Velocity Distribution
27
27 Outline FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Introduction Objectives State of the Art Methodology Results and Discussion Conclusions
28
28 Conclusions FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Flow through Structured Packed Beds
29
29 Conclusions FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Flow through Randomly Packed Beds Good agreement between Ergun’s pressure drop predictions and simulation results were found Velocity distributions were analyzed and three different zones were identified Velocity distributions appear to follow the average local porosity: the length to establish the flow is identical to the length to establish the porosity
30
30 FEUP/IFPEN Direct Numerical Simulation of Fixed-Bed Reactors: Effect of Random Packing Thank you for your attention www.ifpenergiesnouvelles.com
Similar presentations
© 2024 SlidePlayer.com. Inc.
All rights reserved.