TY - JOUR
T1 - Geldart A− particles
T2 - Hydrodynamics of Geldart A magnetite powder with modulation by ultrafine coal particles in Gas-solid Fluidized Bed Coal Beneficiator (GFBCB)
AU - Liu, Chengguo
AU - Zhou, Chenyang
AU - Sun, Zeneng
AU - Duan, Chenlong
AU - Zhu, Jesse
AU - Zhao, Yuemin
N1 - Publisher Copyright:
© 2022 Elsevier B.V.
PY - 2022/8
Y1 - 2022/8
N2 - The Gas-solid Fluidized Bed Coal Beneficiator (GFBCB) is an important technology used in the dry coal beneficiation process, which requires lower bed density and very uniform density distribution. Geldart A− particles, Geldart A magnetite particles “modulated” by a small fraction of Geldart C ultrafine coal particles, is proposed. Fundamental studies are carried out to provide a comprehensive understanding of its hydrodynamics, including the minimum fluidization velocity, bed expansion, and spatial bed density distribution. By adding the ultrafine coal particles, the minimum fluidization velocity (Umf) is lowered, with a modified Umf correlation proposed, the bed expansion drastically increased (by up to 30%), with more gas being retained in the bed for improved flowability, and the corresponding bed density decreased to 1600–2000 kg/m3, with more uniform distribution, all contributing to a more desirable separation environment for coal beneficiation.
AB - The Gas-solid Fluidized Bed Coal Beneficiator (GFBCB) is an important technology used in the dry coal beneficiation process, which requires lower bed density and very uniform density distribution. Geldart A− particles, Geldart A magnetite particles “modulated” by a small fraction of Geldart C ultrafine coal particles, is proposed. Fundamental studies are carried out to provide a comprehensive understanding of its hydrodynamics, including the minimum fluidization velocity, bed expansion, and spatial bed density distribution. By adding the ultrafine coal particles, the minimum fluidization velocity (Umf) is lowered, with a modified Umf correlation proposed, the bed expansion drastically increased (by up to 30%), with more gas being retained in the bed for improved flowability, and the corresponding bed density decreased to 1600–2000 kg/m3, with more uniform distribution, all contributing to a more desirable separation environment for coal beneficiation.
KW - Bed expansion
KW - Density adjustment and distribution
KW - GFBCB
KW - Geldart A particles
KW - Geldart C particle modulation
KW - Minimum fluidization velocity
UR - http://www.scopus.com/inward/record.url?scp=85134804578&partnerID=8YFLogxK
U2 - 10.1016/j.powtec.2022.117753
DO - 10.1016/j.powtec.2022.117753
M3 - Article
AN - SCOPUS:85134804578
SN - 0032-5910
VL - 408
JO - Powder Technology
JF - Powder Technology
M1 - 117753
ER -