Reversal of gulf stream circulation in a vertically vibrated triangular fluidized bed

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Engineering Conferences International ECI Digital Archives Fluidization XV Proceedings 5-26-2016 Reversal of gulf stream circulation in a vertically vibrated triangular fluidized bed E. Cano-Pleite Carlos III University of Madrid; Department of Thermal and Fluid Engineering,Av. de la Universidad 30, Leganés, Madrid, Spain, edcanop@ing.uc3m.es A. Acosta-Iborra Carlos III University of Madrid; Department of Thermal and Fluid Engineering,Av. de la Universidad 30, Leganés, Madrid, Spain F. Hernández-Jiménez Carlos III University of Madrid; Department of Thermal and Fluid Engineering,Av. de la Universidad 30, Leganés, Madrid, Spain C. R. Müller ETH Zürich, Institute of Energy Technology, Laboratory of Energy Science and Engineering, Leonhardstrasse 21, 8092 Zürich, Switzerland Follow this and additional works at: http://dc.engconfintl.org/fluidization_xv Part of the Chemical Engineering Commons Recommended Citation E. Cano-Pleite, A. Acosta-Iborra, F. Hernández-Jiménez, and C. R. Müller, "Reversal of gulf stream circulation in a vertically vibrated triangular fluidized bed" in "Fluidization XV", Jamal Chaouki, Ecole Polytechnique de Montreal, Canada Franco Berruti, Wewstern University, Canada Xiaotao Bi, UBC, Canada Ray Cocco, PSRI Inc. USA Eds, ECI Symposium Series, (2016). http://dc.engconfintl.org/fluidization_xv/157 This Abstract and Presentation is brought to you for free and open access by the Proceedings at ECI Digital Archives. It has been accepted for inclusion in Fluidization XV by an authorized administrator of ECI Digital Archives. For more information, please contact franco@bepress.com.

Reversal of gulf stream circulation in a vertically vibrated triangular fluidized bed E. Cano-Pleite, F. Hernández-Jiménez, A. Acosta-Iborra, C.R. Müller ISE RESEARCH GROUP CARLOS III UNIVERSITY (MADRID, SPAIN) Fluidization XV E. Cano-Pleite

Table of contents 1. Introduction 2. 3. 4. 5. 2

Table of contents 1. Introduction 2. 3. 4. 5. 3

Motivation When vibration energy is introduced in a granular assembly, a great variety of phenomena can appear. The appearance of granular patterns in vibrated beds is not only restricted to square-shaped beds. Aoki et al. (1996) Adding gas to a triangular or conical shaped bed Aerated hoppers or spout fluidized beds. The present work aims at clarifying the effect of injecting gas through the inclined lateral walls of a vibrated pseudo- 2D triangular bed and the identification of the different granular patterns observed. Lu et al. (2012) 4

Motivation When vibration energy is introduced in a granular assembly, a great variety of phenomena can appear. The appearance of granular patterns in vibrated beds is not only restricted to square-shaped beds. Adding gas to a triangular or conical shaped bed Aerated hoppers or spout fluidized beds. Sutkar et al. (2013) The present work aims at clarifying the effect of injecting gas through the inclined lateral walls of a vibrated pseudo- 2D triangular bed and the identification of the different granular patterns observed. Chen et al. (2011) 4

Table of contents 1. Introduction 2. 3. 4. 5. 5

6

Table of contents 1. Introduction 2. 3. 4. 5. 7

PIV (MatPIV) in a relative system of reference that moves with the bed Absolute Relative Correction of the image Overall average solids velocity Phase averaged solids velocity where Gulf stream circulation in a triangular VFB and E. Cano-Pleite 8

Table of contents 1. Introduction 2. 3. 4. 5. 9

General bed behavior Different behaviors were observed depending on the gas superficial velocity and the vibration strength and frequency: Tilting f/2 surface waves f/4 surface waves Downward convection Reversed convection No gas injection Gas injection 10

Transition maps Γ-f transition maps for different gas superficial velocities - Different granular patterns are observed - Regions of reversed gulf stream circulation of particles 11

Solids velocity Formation of arching structures close to the lateral walls of the bed Four stagnation points when the gulf stream circulation of particles is reversed. 12

Solids velocity Formation of arching structures close to the lateral walls of the bed Four stagnation points when the gulf stream circulation of particles is reversed. 12

Solids velocity Formation of arching structures close to the lateral walls of the bed Four stagnation points when the gulf stream circulation of particles is reversed. What is the cause of the convective motions? 12

No gas injection behavior No gas, f = 15 Hz, Γ=3.5 13

No gas injection behavior No gas, f = 15 Hz, Γ=3.5 13

No gas injection behavior No gas, f = 15 Hz, Γ=3.5 Gulf stream circulation in a triangular VFB E. Cano-Pleite 13

No gas injection behavior No gas, f = 15 Hz, Γ=3.5 Gulf stream circulation in a triangular VFB E. Cano-Pleite 13

No gas injection behavior No gas, f = 15 Hz, Γ=3.5 Gulf stream circulation in a triangular VFB E. Cano-Pleite 13

No gas injection behavior No gas, f = 15 Hz, Γ=3.5 Impact of the bed bulk with the inclined walls 13

No gas injection behavior No gas, f = 15 Hz, Γ=3.5 The impact wave propagates from the inclined walls to the central section of the bed. 14

Reversal of gulf stream circulation U 0 /U mf = 1.2, f = 15 Hz, Γ = 3.5 Four subcycles for each cycle of the bed bulk. Two regions: close to the lateral walls and center. Average particle motion reversal of the gulf stream circulation of particles. 15

Reversal of gulf stream circulation U 0 /U mf = 1.2, f = 15 Hz, Γ = 3.5 Four subcycles for each cycle of the bed bulk. Two regions: close to the lateral walls and center. Average particle motion reversal of the gulf stream circulation of particles. Gulf stream circulation in a triangular VFB E. Cano-Pleite 15

Reversal of gulf stream circulation U 0 /U mf = 1.2, f = 15 Hz, Γ = 3.5 Four subcycles for each cycle of the bed bulk. Two regions: close to the lateral walls and center. Average particle motion reversal of the gulf stream circulation of particles. Gulf stream circulation in a triangular VFB E. Cano-Pleite 15

Reversal of gulf stream circulation U 0 /U mf = 1.2, f = 15 Hz, Γ = 3.5 Four subcycles for each cycle of the bed bulk. Two regions: close to the lateral walls and center. Average particle motion reversal of the gulf stream circulation of particles. Gulf stream circulation in a triangular VFB E. Cano-Pleite 15

Reversal of gulf stream circulation U 0 /U mf = 1.2, f = 15 Hz, Γ = 3.5 Four subcycles for each cycle of the bed bulk. Two regions: close to the lateral walls and center. Average particle motion reversal of the gulf stream circulation of particles. Gulf stream circulation in a triangular VFB E. Cano-Pleite 15

Table of contents 1. Introduction 2. 3. 4. 5. 16

Gas injection through the inclined walls of the bed change the way particles behave in a fluidized bed of triangular shape. Different patterns, including tilting, f/2 and f/4 surface waves were observed. The gulf stream circulation of particles in the triangular bed could be reversed when injecting gas through the inclined walls. Several subcycles of vibration appear when gas is injected. The average particle motion after a whole cycle leads to the reversal of the gulf stream circulation. 17

Segregation of equal-sized particles of different densities in a vertically Thank you for your attention This work has been partially funded by the Universidad Carlos III de Madrid (Ayudas a la movilidad 2015) and by the Spanish Ministry of Economy and Competiveness (project ENE2015/00188/001) 18