TY - JOUR
T1 - Inhomogeneity in low pressure fluidization
AU - Weerasiri, Lanka Dinushke
AU - Fabijanic, Daniel
AU - Das, Subrat
N1 - Publisher Copyright:
© 2023 Elsevier B.V.
PY - 2023/3/1
Y1 - 2023/3/1
N2 - Low pressure fluidization has been one of the most promising advances in the fluidization topic since its inception. Its low mass consumption is a key benefit, but equally, it is known for its low fluidization quality due to inhomogeneous fluidization. In this work, an experimental study was conducted to study the cause, mechanism and possible remedies to the inhomogeneous fluidization behaviour at low pressure. A 2D pseudo bed was used to capture the bubbling phenomenon and pressure drop characteristics for alumina powder at a wide range of operating pressures (0 to −98,185 Pa), bed heights (221, 534 and 727 mm) and inlet flow rates (0.1 to 18 l/min). The high pressure differential between the bottom and top of the bed at low pressure was the main cause of the inhomogeneous fluidization behaviour. The pressure differential causes a steep rise in the gas velocity profile within the bed, resulting in the two different fluidization states within the same bed. The bed height, voidage and particle density were found to improve the fluidization quality with some drawbacks. An alternative approach was to increase the bed area with height. This alteration can be used to improve the fluidization quality for any given powder and operating condition.
AB - Low pressure fluidization has been one of the most promising advances in the fluidization topic since its inception. Its low mass consumption is a key benefit, but equally, it is known for its low fluidization quality due to inhomogeneous fluidization. In this work, an experimental study was conducted to study the cause, mechanism and possible remedies to the inhomogeneous fluidization behaviour at low pressure. A 2D pseudo bed was used to capture the bubbling phenomenon and pressure drop characteristics for alumina powder at a wide range of operating pressures (0 to −98,185 Pa), bed heights (221, 534 and 727 mm) and inlet flow rates (0.1 to 18 l/min). The high pressure differential between the bottom and top of the bed at low pressure was the main cause of the inhomogeneous fluidization behaviour. The pressure differential causes a steep rise in the gas velocity profile within the bed, resulting in the two different fluidization states within the same bed. The bed height, voidage and particle density were found to improve the fluidization quality with some drawbacks. An alternative approach was to increase the bed area with height. This alteration can be used to improve the fluidization quality for any given powder and operating condition.
KW - Bubbling bed
KW - High-speed imaging
KW - Inhomogeneous fluidization
KW - Low pressure fluidization
KW - Slip flow regime
UR - https://www.scopus.com/pages/publications/85146616480
U2 - 10.1016/j.powtec.2023.118247
DO - 10.1016/j.powtec.2023.118247
M3 - Article
AN - SCOPUS:85146616480
SN - 0032-5910
VL - 417
JO - Powder Technology
JF - Powder Technology
M1 - 118247
ER -