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A fluidised bed reactor (diameter [url removed, login to view]) has 6000 kg of solid catalyst (bed density is 1000kg/m3, with 50% of the bed occupied by the gas) and is fluidised with gas A (5 bar, 300C). The superficial velocity, the velocity based an empty reactor, u of A is 20 cm/s [url removed, login to view] see attachment

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