Oxy-fuel combustion on circulating fluidized bed (CFB)

Author(s):  
E.J. Anthony ◽  
H. Hack
2008 ◽  
Vol 39 (1) ◽  
pp. 65-78
Author(s):  
Yu. S. Teplitskii ◽  
V. A. Borodulya ◽  
V. I. Kovenskii ◽  
E. P. Nogotov

2019 ◽  
Vol 195 ◽  
pp. 106129 ◽  
Author(s):  
Ying Wu ◽  
Daoyin Liu ◽  
Dong Zheng ◽  
Jiliang Ma ◽  
Lunbo Duan ◽  
...  

Fuel ◽  
2016 ◽  
Vol 170 ◽  
pp. 92-99 ◽  
Author(s):  
Ha-Na Jang ◽  
Jeong-Hun Kim ◽  
Seung-Ki Back ◽  
Jin-Ho Sung ◽  
Heung-Min Yoo ◽  
...  

2012 ◽  
Vol 57 (1) ◽  
pp. 79-92
Author(s):  
Agnieszka Kijo-Kleczkowska

In the paper the problem of heavily-watered fuel combustion has been undertaken as the requirements of qualitative coals combusted in power stations have been growing. Coal mines that want to fulfill expectations of power engineers have been forced to extend and modernize the coal enrichment plants. This causes growing quantity of waste materials that arise during the process of wet coal enrichment containing smaller and smaller under-grains. In this situation the idea of combustion of transported waste materials, for example in a hydraulic way to the nearby power stations appears attractive because of a possible elimination of the necessary deep dehydration and drying as well as because of elimination of the finest coal fraction loss arising during discharging of silted water from coal wet cleaning plants. The paper presents experimental research results, analyzing the process of combustion of coal-water suspension depending on the process conditions. Combustion of coal-water suspensions in fluidized beds meets very well the difficult conditions, which should be obtained to use the examined fuel efficiently and ecologically. The suitable construction of the research stand enables recognition of the mechanism of coal-water suspension contact with the inert material, that affects the fluidized bed. The form of this contact determines conditions of heat and mass exchange, which influence the course of a combustion process. The specificity of coal-water fuel combustion in a fluidized bed changes mechanism and kinetics of the process.


2014 ◽  
Vol 31 (6) ◽  
pp. 638-645
Author(s):  
Jin-Ho Sung ◽  
◽  
Yong-Chil Seo ◽  
Ha-Na Jang ◽  
Seung-Ki Back ◽  
...  

2011 ◽  
Vol 88 (9) ◽  
pp. 2940-2948 ◽  
Author(s):  
Yinghai Wu ◽  
Chunbo Wang ◽  
Yewen Tan ◽  
Lufei Jia ◽  
Edward J. Anthony

2016 ◽  
Vol 20 (suppl. 1) ◽  
pp. 1-18 ◽  
Author(s):  
Bo Leckner

A summary is given on the development of fluidized bed conversion (combustion and gasification) of solid fuels. First, gasification is mentioned, following the line of development from the Winkler gasifier to recent designs. The combustors were initially bubbling beds, which were found unsuitable for combustion of coal because of various drawbacks, but they proved more useful for biomass where these drawbacks were absent. Instead, circulating fluidized bed boilers became the most important coal converters, whose design now is quite mature, and presently the increments in size and efficiency are the most important development tasks. The new modifications of these conversion devices are related to CO2 capture. Proposed methods with this purpose, involving fluidized bed, are single-reactor systems like oxy-fuel combustion, and dual-reactor systems, including also indirect biomass gasifiers.


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