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IbD PU Deliverable 3.1 Figure 10. The spinning cone concept (Hetherington et al., 2001). In the research of Wagenaar et al. (1994), particle dynamics and gas-phase hydrodynamics in a SCR was studied as a first stage to understand the performance of SCR which could be used for rapid thermal solid processing. The solids processing in the reactor was influenced by operational and physical parameters of the reactor, such as the cone rotational speed, the particle diameter, and the cone top-angles. The residence time and shape of the trajectories of particles were independent of the particle diameter if the particles had a large diameter (larger than 400 μm in their case). The motion of smaller particles (less than 200 μm in their case) was highly influenced by the gas flow in the SCR. Hetherington et al. (2001) used the SCR for the precipitation of barium sulphate. Smaller crystal sizes were consistently obtained in the SCR in comparison to batch processing, with increases in the cone rotational speed exerting a significant influence on the crystal size. 4.3 Rotating packed/fluidized beds 4.3.1 Rotating packed beds The rotating packed bed (RPB) is another process intensified equipment which is based on the high centrifugal acceleration technique. In contrast to the spinning disk or cone, it consists of an enclosed volume packed with structured packings of higher specific surface area 14PDF Image | Solids handling for intensified process technology
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