scholarly journals Chemical-looping combustion in packed-fluidized beds: Experiments with random packings in bubbling bed

2021 ◽  
Vol 222 ◽  
pp. 106978
Author(s):  
Nasrin Nemati ◽  
Magnus Rydén
2019 ◽  
Vol 33 (5) ◽  
pp. 4442-4453 ◽  
Author(s):  
Jesper Aronsson ◽  
Ewa Krymarys ◽  
Viktor Stenberg ◽  
Tobias Mattisson ◽  
Anders Lyngfelt ◽  
...  

2018 ◽  
Vol 140 (11) ◽  
Author(s):  
Johannes George van der Watt ◽  
Daniel Laudal ◽  
Gautham Krishnamoorthy ◽  
Harry Feilen ◽  
Michael Mann ◽  
...  

We have investigated a novel gas/solid contacting configuration for chemical looping combustion (CLC) with potential operating benefits. CLC configurations are typically able to achieve high fuel conversion efficiencies at the expense of high operating costs and low system reliability. The spouted fluid bed (SB) was identified as an improved reactor configuration for CLC, since it typically exhibits high heat transfer rates and offers the ability to use lower gas flows for material movement compared to bubbling beds (BB). Multiphase Flow with Interphase eXchanges (MFIX) software was used to establish a spouted fluid bed reactor design. An experimental setup was built to supplement the model. The experimental setup was also modified for testing under high temperature, reacting conditions (1073–1273 K). The setup was operated in either a spouted fluid bed or a bubbling bed regime to compare the performance attributes of each. Results for the reactor configurations are presented for CLC using a mixture of carbon monoxide and hydrogen as fuel. Compared to the bubbling bed, the spouted fluid bed reactor achieved an equivalent or better fuel conversion at a lower pressure drop over the material bed. The spouted fluid bed design represents a viable configuration to improve gas/solid contacting for efficient fuel conversion, lower energy requirements for material movement and increase operational robustness for CLC. The research laid the groundwork for future research into a multi-phase reacting flow CLC system. The system will be developed from computational fluid dynamic modeling and pilot-scale testing to expedite the development of CLC technologies.


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.


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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