Flow characteristics of a small moving bed downcomer with an orifice under negative pressure gradient

Behaviour of gas–solid mixtures in a small moving bed downcomer operating under negative pressure gradient has been investigated experimentally, because flow characteristics in a downcomer are important factors in powder handling processes, such as a multi-stage spouted bed or a circulating fluidized bed. In this study, a small downcomer in which the moving bed height could be controlled was employed with the intention of using a downcomer as a connecting tube in a multi-stage spouted bed. Based on experimental observation, the moving bed flow changed from smooth flow (Region(I)) to slip-stick flow (Region(II)) and then changed from slip-stick flow to intermittent flow (Regime(III)), as the gas pressure gradient in the downcomer was increased. In this study, the critical point for steady-state (Region(I)) operation was also examined experimentally and theoretically, by using eight kinds of solid particles (Geldart B, D and A powders) and six different orifice sizes which were used to restrict solids flow at the base of the downcomer. As a result, a correlation of solids flow rate in the stable moving bed downcomer under negative pressure gradient was derived and the critical point between stable and unstable flow was explained by the proposed model.

Behaviour of gas–solid mixtures in a moving bed downcomer operating under negative pressure gradient was investigated experimentally.The solids flow could be divided into three patterns (stable, unstable and intermittent flow). A correlation of solids flow rate in the stable moving bed downcomer was derived and the critical point of stable moving bed flow was explained by a model.Figure optionsDownload as PowerPoint slide