Dry Desulfurization of Simulated Flue Gas in a Fluidized-Bed Reactor for a Broad Range of SO2Concentration and Temperature:  A Comparison of Models

1999 ◽  
Vol 38 (8) ◽  
pp. 2932-2939 ◽  
Author(s):  
Y. Suyadal ◽  
H. Oguz
Keyword(s):  
Fluidized Bed ◽  
Flue Gas ◽  
Fluidized Bed Reactor

scholarly journals Flying MOFs: polyamine-containing fluidized MOF/SiO2 hybrid materials for CO2 capture from post-combustion flue gas

2018 ◽  
Vol 9 (20) ◽  
pp. 4589-4599 ◽  
Author(s):  
Ignacio Luz ◽  
Mustapha Soukri ◽  
Marty Lail
Keyword(s):  
Solid State ◽  
Mesoporous Silica ◽  
Fluidized Bed ◽  
Hybrid Materials ◽  
Flue Gas ◽  
Metal Organic Framework ◽  
Fluidized Bed Reactor ◽  
Large Collection ◽  
Solid Sorbents ◽  
Metal Organic

Solid-state synthesis ensures a high loading and well dispersed growth of a large collection of metal–organic framework (MOF) nanostructures within a series of commercially available mesoporous silica allowing to render MOFs into fluidized solid sorbents for CO2 capture from post-combustion flue gas in a fluidized-bed reactor.

scholarly journals Carbon Shale Combustion in the Fluidized Bed Reactor

2014 ◽  
Vol 16 (2) ◽  
pp. 74-76 ◽  
Author(s):  
Małgorzata Olek ◽  
Stanisław Kandefer ◽  
Wiesław Kaniowski ◽  
Witold Żukowski ◽  
Jerzy Baron
Keyword(s):  
Fluidized Bed ◽  
Flue Gas ◽  
Combustion Process ◽  
Fluidized Bed Reactor ◽  
Ash Content ◽  
Conversion Degree ◽  
Hard Coal ◽  
Combustible Material ◽  
High Quality ◽  
Bubbling Fluidized Bed

Abstract The purpose of this article is to present the possibilities of coal shale combustion in furnaces with bubbling fluidized bed. Coal shale can be autothermally combusted in the fluidized bed, despite the low calorie value and high ash content of fuel. Established concentrations of CO (500 ppm) and VOC (30 mg/m3) have indicated a high conversion degree of combustible material during combustion process. Average concentrations of SO2 and NOx in the flue gas were higher than this received from the combustion of high quality hard coal, 600 ppm and 500 ppm, respectively. Optional reduction of SO2 and NOx emission may require the installation of flue gas desulphurization and de-NOx systems.

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