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Abstract
This work extends the Pitot-tube probe technique to the study of jetting phenomena in a three-dimensional, high-temperature gas-solid fluidized bed. For an isolated jet, the jet height was defined as the intersection of two momentum flux profiles, one along the jet axis and the other in the emulsion phase. A study of two adjacent jets confirmed that the measured jet heights were close to the visual jet heights observed through a window in the bed.
In two adjacent jets, the jets behave like two isolated jets at low nozzle velocities. As the nozzle velocity increases, the jet heights reach a maximum height in the transition zone. The jets begin to interact after the transition zone, and the jet height becomes a constant.
Similar results are obtained for two kinds of perforated-plate distributors. The maximum jet height for multiple, interacting jets is a function only of distributor geometry and is well predicted by a simple geometric model.