Preparation method for synthesizing sheet-type cladding material by fluidized bed gas-phase method
A technology for coating materials and sheet materials, which is applied in the field of preparation of sheet-shaped coating materials synthesized by fluidized bed gas phase method, can solve the problems of high process requirements and insufficient recycling of fluidization gas, and achieve operational steps Simple, highly reproducible, effects that improve or alter dispersion
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Embodiment 1
[0028] a. Weigh 450 g of flaky mica (conical or cylindrical) with an average particle size of 30 μm and an aspect ratio of 31, and place it in the cavity of the fluidized bed reactor through the feeding port at the upper end of the fluidized bed reactor bottom;
[0029] b. Turn on the vacuum pump to evacuate the chamber of the fluidized bed reactor, inject fluidizing gas nitrogen from the inlet of the fluidizing gas, determine the flow rate through the pressure gauge, turn on the gas circulation pump to circulate the fluidizing gas, and adjust the fluidizing gas Airflow at 3.0 m 3 / h, so that the flake mica is in suspension;
[0030] c. Adjust the temperature of the heating furnace body to 550°C so that the reactor cavity is at a stable temperature;
[0031] d. The liquid orthosilicate is sucked into the liquid vaporizer from the liquid storage tank through the liquid sampling pump, and after being vaporized at 170°C, it is passed into the cavity of the fluidized bed reactor...
Embodiment 2
[0036] a. Take by weighing 450 g of flake mica with an average particle diameter of 30 μm, and place it at the bottom of the fluidized bed reactor chamber through the feed port at the upper end of the reactor;
[0037] b. Turn on the vacuum pump to evacuate the chamber of the fluidized bed reactor, inject the fluidizing gas nitrogen from the inlet of the fluidizing gas, determine the flow rate through the pressure gauge, turn on the circulating pump to circulate the fluidizing gas, and adjust the flow of the fluidizing gas 3.0 m in size 3 / h, make the flake mica in suspension;
[0038] c. Adjust the temperature of the heating furnace body to 525°C, so that the reactor cavity is at a stable temperature;
[0039] d. The liquid tetrabutyl titanate is sucked into the liquid vaporizer from the liquid storage tank through the liquid sampling pump, and after being vaporized at 315°C, it is passed into the fluidized bed reactor at a rate of 0.3 g / min;
[0040]e. Under the action of ...
Embodiment 3
[0044] a. Take by weighing 450 g of flake mica with an average particle diameter of 30 μm, and place it at the bottom of the fluidized bed reactor chamber through the feed port at the upper end of the reactor;
[0045] b. Turn on the vacuum pump to evacuate the chamber of the fluidized bed reactor, inject the fluidizing gas nitrogen from the inlet of the fluidizing gas, determine the flow rate through the pressure gauge, turn on the circulating pump to circulate the fluidizing gas, and adjust the flow of the fluidizing gas 3.6 m in size 3 / h, so that the flake mica is in suspension;
[0046] c. Adjust the temperature of the heating furnace body to 350°C, so that the reactor cavity is at a stable temperature;
[0047] d. The toluene solution of triisobutylaluminum with a mass fraction of 25% is sucked from the liquid storage tank 1 into the liquid vaporizer 1 through the liquid sampling pump, and is gasified at 160°C and then passed into the fluidized bed at a rate of 2.6 g / mi...
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