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Simulations indicated that the gas volume fraction of coal particle cluster increases with time after devolatilization.
The shrinkage of a closed pore in the sintering of a particle cluster was analyzed.
The origin of phenomena is believed to be due to the collective resonance excitation in the dielectric particle cluster.
Parameters explored are particle area fraction, particle settling speed, particle cluster mobility and grain nucleation rate under continuous nucleation conditions.
On the strength of these experimental data, particle cluster drag coefficients are calculated as a function of the cluster Reynolds' number and average particle number in the cluster.
The Chemical Reactor Engineering Center – Gas Solid – Optiprobes (CREC-GS-Optiprobe) can be used to determine particle cluster properties in down flow reactors.
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During acceleration, particle clusters are gradually disaggregated into smaller clusters with increasing voidage, while during deceleration, particle clusters are aggregated into larger clusters with decreasing voidage.
This model considers the effects of Brownian motion, interfacial layer formation and particle clustering.
Particle clustering is a phenomenon of importance in many applications in gas solid fluidized beds.
Moreover, this kind of dynamic particle aggregation might lead to particle clusters, and investigations of the particle motion and mixing behavior in the simulated systems indicate that there are particle clusters during fluidization.
Particle clustering has long been a focus in the study of gas solid flow.
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