TY - JOUR
T1 - Attrition of high ash Ekibastuz coal in a bench scale fluidized bed rig under O2/N2 and O2/CO2 environments
AU - Suleimenova, Botakoz
AU - Aimbetov, Berik
AU - Shah, Dhawal
AU - Anthony, Edward J.
AU - Sarbassov, Yerbol
N1 - Funding Information:
This research was funded by the Nazarbayev University (NU) , Project number SOE2019011 : “Co-firing of coal and biomass under air and oxy-fuel environments in fluidized bed rig: Experiments with process model development” and Grant number № 3-2020/003-2020 entitled: “Development of municipal solid waste combustion and incineration technology and investigation of co-firing of municipal solid waste and coal in CFB”.
Publisher Copyright:
© 2021 Elsevier B.V.
PY - 2021/6/1
Y1 - 2021/6/1
N2 - While fluidized bed coal combustion technology has advanced significantly, attrition and its impact on combustion remains a problem. Using a bench scale fluidized bed unit, we examined the experimental attrition data for batches of coal ash particles. Experiments were carried out in the presence of bed material (sand) by adding coal particle to the hot riser, which has a height of 500 mm and internal diameter of 25.4 mm. Combustion of coal particles with high ash content was carried out in both O2/N2 and O2/CO2 environments. Coal particles with sizes of 0.4–0.8 mm and 0.8–1.4 mm were prepared by sieving and examined in this work. Using this data, the effect of critical factors on attrition such as gas velocity, particle size, and combustion environments were analyzed. In addition, the composition of ash particles was analyzed by SEM/EDX and XRF. The sizes of ash particles were less than 0.2 mm after combustion. A higher attrition rate was determined at higher gas velocity, regardless of the combustion environment. The ash composition analysis showed high concentration of silicon and aluminum oxide in the ash, and this possibly was increased due to kaolinite decomposition.
AB - While fluidized bed coal combustion technology has advanced significantly, attrition and its impact on combustion remains a problem. Using a bench scale fluidized bed unit, we examined the experimental attrition data for batches of coal ash particles. Experiments were carried out in the presence of bed material (sand) by adding coal particle to the hot riser, which has a height of 500 mm and internal diameter of 25.4 mm. Combustion of coal particles with high ash content was carried out in both O2/N2 and O2/CO2 environments. Coal particles with sizes of 0.4–0.8 mm and 0.8–1.4 mm were prepared by sieving and examined in this work. Using this data, the effect of critical factors on attrition such as gas velocity, particle size, and combustion environments were analyzed. In addition, the composition of ash particles was analyzed by SEM/EDX and XRF. The sizes of ash particles were less than 0.2 mm after combustion. A higher attrition rate was determined at higher gas velocity, regardless of the combustion environment. The ash composition analysis showed high concentration of silicon and aluminum oxide in the ash, and this possibly was increased due to kaolinite decomposition.
KW - Ash composition
KW - Attrition rate
KW - Bituminous coal
KW - Fluidized bed
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U2 - 10.1016/j.fuproc.2021.106775
DO - 10.1016/j.fuproc.2021.106775
M3 - Article
AN - SCOPUS:85100804471
SN - 0378-3820
VL - 216
JO - Fuel Processing Technology
JF - Fuel Processing Technology
M1 - 106775
ER -