Core-shell structure nanometer composite particle as well as preparation method and preparation device thereof
A core-shell structure and nanocomposite technology, applied in nanocarbon, nanotechnology, nanotechnology and other directions, can solve the problems of low preparation temperature, inability to prepare materials, particle aggregation, etc., to achieve simple process operation, simple process flow, continuous production. Effect
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Embodiment 1
[0043] Example 1 Preparation of composite particles from precursors from different sources
[0044] Proceed as follows:
[0045] (1) Hexamethyldisilane, the precursor of the core material, was heated to 80°C by heating in a water bath, hydrogen was used as the carrier gas, and the flow rate of the carrier gas was 0.6L / min;
[0046] (2) After mixing the shell material precursor propylene and the core material precursor, pass it into the fluidized bed reactor from the bottom, and the flow rate of propylene is 2.0L / min;
[0047] (3) The mixed gas of hydrogen and argon is used as the fluidization gas, the flow rate of hydrogen is 1.2L / min, and the flow rate of argon is 1.5L / min;
[0048] The fluidized bed reactor is heated to 1000°C to start the reaction, and the powder is collected through the powder collection system at the top of the reactor.
[0049] The obtained powder product is a core-shell structure particle with silicon carbide as the core structure and elemental carbon...
Embodiment 2
[0050] Example 2 Preparation of composite particles from precursors from different sources
[0051] Proceed as follows:
[0052] (1) Hexamethyldisilane, the precursor of the core material, is heated to 80°C by heating in a water bath, hydrogen is used as the carrier gas, and the flow rate of the carrier gas is 0.6L / min, and it enters the fluidized bed reactor from the bottom ;
[0053] (2) Heat the aluminum sec-butoxide precursor of the shell material to 150°C by electric heating, use argon as the carrier gas, and the flow rate of the carrier gas is 1.5L / min, and enter the fluidized bed reactor from the top;
[0054] (3) The mixed gas of hydrogen and argon is used as the fluidization gas, the flow rate of hydrogen is 1.2L / min, and the flow rate of argon is 1.5L / min;
[0055] Heat the fluidized bed reactor to 1100°C to start the reaction, and collect the powder through the powder collection system at the top of the reactor;
[0056] (4) The obtained powder was heat-treated a...
Embodiment 3
[0058] Example 3 Preparation of Composite Particles from Different Sources of Precursors
[0059] Proceed as follows:
[0060] (1) Heat the core material precursor aluminum sec-butoxide to 150°C by electric heating, use argon as the carrier gas, the flow rate of the carrier gas is 1.0L / min, and enter the fluidized bed reactor from the bottom;
[0061] (2) Heat copper acetylacetonate, the precursor of the shell material, to 160°C by electric heating, use argon as the carrier gas, and the flow rate of the carrier gas is 0.3L / min, and enter the fluidized bed reactor from the side wall;
[0062] (3) The mixed gas of hydrogen and argon is used as the fluidization gas, the flow rate of hydrogen is 0.8L / min, and the flow rate of argon is 1.5L / min;
[0063] Heat the fluidized bed reactor to 900°C to start the reaction, and collect the powder through the powder collection system at the top of the reactor;
[0064] (4) The obtained powder was heat-treated at 800° C. for 1 hour under a...
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