Zobrazeno 1 - 7
of 7
pro vyhledávání: '"PARTICLE TECHNOLOGY AND FLUIDIZATION"'
Funder: The University of Queensland
Spheronization of cylindrical extrudates on a rotating friction plate involves breakage and rounding. Little attention has been given to the breakage stage and quantitative modeling of this process is scarce.
Spheronization of cylindrical extrudates on a rotating friction plate involves breakage and rounding. Little attention has been given to the breakage stage and quantitative modeling of this process is scarce.
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::65dcce7dc3ce9935c872187cd9aa76da
Autor:
Ivan Mema, JT Johan Padding
Publikováno v:
AIChE Journal, 67(5)
Aiche Journal. American Institute of Chemical Engineers
Aiche Journal. American Institute of Chemical Engineers
Having proper correlations for hydrodynamic forces is essential for successful CFD‐DEM simulations of a fluidized bed. For spherical particles in a fluidized bed, efficient correlations for predicting the drag force, including the crowding effect c
Publikováno v:
Aiche Journal. American Institute of Chemical Engineers
AIChE Journal, 64(5)
AIChE Journal, 64(5)
Fluidization is widely used in industries and has been extensively studied, both experimentally and theoretically, in the past. However, most of these studies focus on spherical particles while in practice granules are rarely spherical. Particle shap
Publikováno v:
AIChE Journal, 63(12), 5335-5342. American Institute of Chemical Engineers (AIChE)
AIChE Journal, 63(12)
Aiche Journal. American Institute of Chemical Engineers
AIChE Journal, 63(12)
Aiche Journal. American Institute of Chemical Engineers
In granular flow operations, often particles are nonspherical. This has inspired a vast amount of research in understanding the behavior of these particles. Various models are being developed to study the hydrodynamics involving nonspherical particle
Publikováno v:
Aiche Journal. American Institute of Chemical Engineers
Coincident (simultaneous) three‐component particle velocity measurements performed using two laser Doppler anemometry probes at the outlet section of a 9 m high cylindrical riser are for the first time presented for dilute flow conditions. Near the
Publikováno v:
Aiche Journal. American Institute of Chemical Engineers
A unique normalized radial pressure profile characterizes the bed of a gas‐solid vortex reactor over a range of particle densities and sizes, solid capacities, and gas flow rates: 950–1240 kg/m3, 1–2 mm, 2 kg to maximum solids capacity, and 0.4
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