Improved Gas–Solids Mass Transfer in Fluidized Beds: Confined Fluidization in Chemical-Looping Combustion

2019 ◽  
Vol 33 (5) ◽  
pp. 4442-4453 ◽  
Author(s):  
Jesper Aronsson ◽  
Ewa Krymarys ◽  
Viktor Stenberg ◽  
Tobias Mattisson ◽  
Anders Lyngfelt ◽  
...  
2011 ◽  
Vol 92 (3) ◽  
pp. 385-393 ◽  
Author(s):  
Wang Shuai ◽  
Liu Guodong ◽  
Lu Huilin ◽  
Chen Juhui ◽  
He Yurong ◽  
...  

2015 ◽  
Vol 138 (4) ◽  
Author(s):  
Ronald W. Breault ◽  
Cory S. Yarrington ◽  
Justin M. Weber

For chemical looping processes to become an economically viable technology, an inexpensive carrier that can endure repeated reduction and oxidation cycles needs to be identified or developed. Unfortunately, the reduction of hematite ore with methane in both batch and fluidized beds has revealed that the performance (methane conversion) decreases with time. Previous analysis had shown that the grains within the particle grew with the net effect of reducing the surface area of the particles and thereby reducing the rate and net conversion for a fixed reduction time. To improve the lifespan of hematite ore, it is hypothesized that if the grain size could be stabilized, then the conversion could be stabilized. In this work, series of tests were conducted in an electrically heated fluidized bed. The hematite ore was first pretreated at a temperature higher than the subsequent reduction temperatures. After pretreatment, the hematite ore was subjected to a series of cyclic reduction/oxidation experiments. The results show that the ore can be stabilized for cycles at different conditions up to the pretreatment temperature without any degradation. Details of the pretreatment process and the test results will be presented.


Energies ◽  
2021 ◽  
Vol 14 (19) ◽  
pp. 6059
Author(s):  
Vlad-Cristian Sandu ◽  
Ana-Maria Cormos ◽  
Calin-Cristian Cormos

As global power generation is currently relying on fossil fuel-based power plants, more anthropogenic CO2 is being released into the atmosphere. During the transition period to alternative energy sources, carbon capture and storage seems to be a promising solution. Chemical-looping combustion (CLC) is an energy conversion technology designed for combustion of fossil fuel with advantageous carbon capture capabilities. In this work, a 1D computational fluid dynamics (CFD) multiscale model was developed to study the reduction step in a syngas-based CLC system and was validated using literature data (R=0.99). In order to investigate mass transfer effects, flow rate and particle dimension studies were carried out. Sharper mass transfer rates were seen at lower flow rates and smaller granule sizes due to suppression of diffusion limitations. In addition, a 3D CFD particle model was developed to investigate in depth the reduction within an ilmenite particle, with focus on heat transfer effects. Minor differences of 1 K were seen when comparing temperature changes predicted by the two models during the slightly exothermic reduction reaction with syngas.


2007 ◽  
Vol 50 (2) ◽  
pp. 230-240 ◽  
Author(s):  
LaiHong Shen ◽  
Min Zheng ◽  
Jun Xiao ◽  
Hui Zhang ◽  
Rui Xiao

2018 ◽  
Vol 32 (12) ◽  
pp. 12721-12729 ◽  
Author(s):  
Shouxi Jiang ◽  
Laihong Shen ◽  
Jingchun Yan ◽  
Huijun Ge ◽  
Tao Song

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