A fluidized bed chemical vapor deposition preparation method of silicon carbide nanowires
A technology of silicon carbide nanowires and chemical vapor deposition, applied in the direction of nanotechnology, nanotechnology, nanotechnology for materials and surface science, etc., to achieve the effect of convenient process operation, simple process flow, and continuous production
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Embodiment 1
[0037] Use H 2 is the fluidizing gas, H 2 The flow rate is 6L / min, 40g ZrO 2 - CoO (the mass fraction of CoO is 6%) particles are placed in a fluidized bed at 1300° C. for fluidization, and the average diameter of the particles is 600 μm. Methyltrichlorosilane is kept at 35°C, and the temperature is continuously raised to 1500°C to pass through methyltrichlorosilane, H 2 It is the carrier gas, the flow rate of the carrier gas is 0.3L / min, and the reaction time is 1h.
[0038] The XRD spectrum of the reaction product is as figure 2 As shown, by comparing the standard card, it can be seen that the product is silicon carbide in the cubic phase, and there is no other impurity phase. Scanning electron microscope and transmission electron microscope photos of SiC nanowires such as image 3 , Figure 4 As shown, it can be seen that the purity of the nanowires is high (no nanoparticles or other forms of silicon carbide), the length of the nanowires is in the range of hundreds o...
Embodiment 2
[0040] Use H 2 is the fluidizing gas, H 2 The flow rate is 3L / min, and 20g metal Fe particles are placed in a fluidized bed at 1300°C for fluidization, with an average particle diameter of 200μm. Methyltrichlorosilane is kept at 35°C, and the temperature is continuously raised to 1400°C, and methyltrichlorosilane is passed through, H 2 As the carrier gas, the flow rate of the carrier gas is 0.15 L / min. After 1 hour of reaction time, 20 g of metal Fe particles are added through the inlet of the fluidized bed, and the reaction is continued for 1 hour.
Embodiment 3
[0042] Using Ar and H 2 The mixed gas is fluidizing gas, the flow rate of Ar is 0.85L / min, H 2 The flow rate is 6L / min, 40g ZrO 2 - CoO (the mass fraction of CoO is 6%) particles are placed in a fluidized bed at 1300° C. for fluidization, and the average diameter of the particles is 800 μm. Methyltrichlorosilane is kept at 35°C, and the temperature is continuously raised to 1580°C, and methyltrichlorosilane is passed through, H 2 It is the carrier gas, the flow rate of the carrier gas is 0.3L / min, and the reaction time is 1h.
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