A device and method for melting and spraying granulation of proliferating agent ceramic pellets
A technology of spray granulation and proliferation agent, which is applied in the direction of liquid droplet granulation, etc., can solve the problems of reducing mechanical properties, cost consumption, low pellet yield, etc., to improve the poor particle size distribution and reduce the difficulty of collection. , the effect of reducing the chance of breaking
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Embodiment 1
[0050] The ratio of the length of the furnace to the length of the pressure tube is 1.5, the inner diameter of the dropper is 0.5 mm, and the vertical distance between the bottom surface of the collector and the outlet of the dropper is 5m. First, add the proliferating agent powder from the pressure tube into the furnace, and use electromagnetic induction to heat the proliferating agent to 1300°C-1600°C in the furnace, so that the proliferating agent powder becomes a molten proliferating agent liquid; Inert gas N under pressure of 100kPa 2 , to press the proliferating agent liquid to drop from the dropper to form proliferating agent droplets; the pressurizing device II will inert gas N 2 The inert gas N in the blowing pipe is passed into the blowing pipe 2 The flow rate is 5L / min, and the droplets of the proliferating agent are blown into uniform small droplets, which diverge outward in a conical shape; the pressurization device III blows the inert gas N 2 The inert gas blow...
Embodiment 2
[0052] The implementation steps of embodiment 2 and embodiment 1 are basically the same, and the main difference is that the length ratio of the length of the furnace to the pressure tube is 1.8, the inner diameter of the dropper is 0.8mm, and the vertical distance between the bottom surface of the collector and the outlet of the dropper is 8m , Pressurization device I pressurizes the inert gas Ar of 150kPa, the inert gas N in the blowing pipe 2 The flow rate is 8L / min. 85% of the proliferating agent ceramic balls obtained by the method have a particle size between 0.6 mm and 1.2 mm.
Embodiment 3
[0054] The implementation steps of embodiment 3 and embodiment 1 are basically the same, and the main difference is that the length ratio of the length of the furnace to the pressure tube is 2.0, the inner diameter of the dropper is 1.2mm, and the vertical distance between the bottom surface of the collector and the outlet of the dropper is 10m , Pressurization device I pressurized 200kPa inert gas He, inert gas N in the blowing pipe 2 The flow rate is 10 L / min. 89% of the proliferating agent ceramic balls obtained by the method have a particle size between 0.6 mm and 1.2 mm.
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