System and method for preparing TiN, TiC and TiCN powder in fluidized bed
A fluidized bed and powder technology, which is applied in the fields of materials and chemicals, can solve the problems of lack of low-cost and high-efficiency complete sets of processes, and achieve the effects of controllable shape, simple process, and economical raw materials
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Embodiment 1
[0050] combine figure 1 , the system for preparing TiN, TiC, and TiCN powders used in this example includes a powder feeding device 1, a TiCl 4 Evaporation device 2, heating device 2-1, pre-reaction fluidized bed 3, first cyclone separation device 4, first high-temperature dust removal device 5, evaporation reaction fluidized bed 6, powder recovery device 7, deposition reaction fluidized bed 8 , the second cyclone separation device 9, the second high temperature dedusting device 10, the first water cooling device 11, the powder collecting device 12, the second water cooling device 13, TiCl 4 Recovery device 14, tail gas treatment device 15;
[0051] The air inlet at the bottom of the powder feeding device 1 is connected to the inert gas pipeline through an air valve and the pipeline; The valve is connected to the pipeline; the feed port of the powder feeding device 1 is connected to the discharge port of the powder recovery device 7 through the material valve and the pipelin...
Embodiment 2
[0061] In this embodiment, the method for preparing TiN, TiC, and TiCN powders using the system in the above-mentioned embodiment 1 specifically includes the following steps:
[0062] After the titanium-containing powder is cleaned by inert gas in the powder feeding device 1, it is transported to the pre-reaction fluidized bed 3 through a material valve; hydrogen and inert gas pass through the TiCl 4 Evaporation device 2 gaseous TiCl 4 Loaded into the pre-reaction fluidized bed 3; the inert gas entering the bottom of the pre-reaction fluidized bed 3 keeps the titanium-containing powder in a fluidized state, and obtains a pre-reaction product powder through pre-reaction; the pre-reaction product The powder enters the evaporation reaction fluidized bed 6 through the discharge port of the pre-reaction fluidized bed 3 , the discharge port of the first cyclone separation device 4 and the discharge port of the first high-temperature dust removal device 5 The pre-reaction product po...
Embodiment 3
[0065] In this embodiment, on the basis of the above-mentioned implementation example 2, the titanium-containing powder in the powder feeding device 1 is TiH 2 powder with a purity of 99% and a particle size of 5 μm; the nitrogen source gas is N 2 , H 2 with N 2 The molar ratio is 1 / 6; the TiCl 4 The temperature of the evaporation device 2 is 30°C; the pre-reaction temperature in the pre-reaction fluidized bed 3 is 500°C, wherein TiCl 4 with TiH 2 The molar ratio of the powder is 0.5, the average residence time of the powder is 5min; the gasification temperature of the evaporation reaction fluidized bed 6 is 600°C; the powder synthesis temperature of the deposition reaction fluidized bed 8 is 730°C, and the powder The average residence time is 5min, and the N content in the nitrogen source gas in the deposition reaction fluidized bed 8 is the same as that of the TiCl in the pre-reaction fluidized bed 3 4 The molar ratio is 0.25, figure 2 In order to prepare the SEM scan...
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Abstract
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