A fluidizable bed of granular material is contained in a vessel having a perforated base, which base is separated from the fluidizable bed by a static layer of granular refractory material, the interstices of the static layer being such that the fluidizable bed, though resting on the static layer, shows no tendency to penetrate the static layer appreciably. The static layer may be inhibited from being fluidized either by having a density and a particle size such that an ascending stream of gas is incapable of displacing it or by a mesh covering it. The openings of the mesh permit contact between static layer and fluidizable bed. In the examples (1) fluidizable aluminosilicate particles having a density of 28 lbs./ft3 and a mean diameter of 53 microns are supported on a static layer of silica sand particles having a density of 94,3 lbs./ft.3 and a diameter of 250-350 microns; (2) the silica sand of Example 1 is fluidized on a static layer of bauxite particles having a density of 106 lbs.ft.3 and a mean diameter of 1,000 microns; and (3) Al2O3 particles of density 65,1 lbs./ft.3 and diameter 50-100 microns are supported on a static layer of bauxite as used in Example 2.
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机译:粒状材料的可流化床容纳在具有带孔底部的容器中,该底部通过粒状耐火材料的静态层与流化床隔开,该静态层的空隙使得流化床虽然搁置在静态层,没有表现出明显渗透静态层的趋势。可以通过具有一定的密度和粒径以使上升的气流无法置换该静态层或通过覆盖该丝网的网眼来抑制该静态层的流化。筛孔允许静态层和流化床接触。在实施例(1)中,将密度为28 lbs./ft3,平均直径为53微米的可流化铝硅酸盐颗粒负载在密度为94.3 lbs./ft.3的石英砂颗粒的静态层上。直径为250-350微米; (2)将实施例1的硅砂流化在密度为106lbs.ft.3且平均直径为1,000微米的铝土矿静态层上; (3)如实施例2中所用,将密度为65.1磅/英尺3,直径为50-100微米的Al 2 O 3颗粒负载在铝土矿的静态层上。
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