A method for the efficient and continuous preparation of carbon nanotubes in a coupled fluidized bed
A carbon nanotube and fluidized bed technology, applied in chemical instruments and methods, carbon compounds, inorganic chemistry, etc., can solve the problems of long operating time of carbon nanotubes, broken catalyst particles, low efficiency, etc., to avoid the concentration of reactants Effects of uneven distribution, avoiding temperature distribution, and saving operating time
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Embodiment 1
[0020] This embodiment provides an efficient and continuous preparation method for carbon nanotubes in a coupled fluidized bed, the process is as follows figure 1 As shown, the specific steps are as follows:
[0021] The catalyst 1 is continuously and uniformly sent to the catalyst reduction and activation reactor 102 made of a metal material with good thermal conductivity through the screw conveying method 101. The temperature of the catalyst reduction and activation reactor 102 is controlled between 350 and 650 °C. Put the mixed gas 2 of hydrogen and nitrogen or argon into the catalyst reduction and activation reactor 102, the volume ratio of hydrogen and nitrogen or argon in the mixed gas is 1:0.5-2.0, and keep the reduction and activation reaction space velocity at 1-15h -1 , The gas linear velocity is 0.05-2.0m / s.
[0022] At the bottom side of the catalyst reduction and activation reactor 102, there is a pneumatically opened plate type sealing valve 103, which is period...
Embodiment 2
[0026] This embodiment provides an efficient and continuous preparation method for carbon nanotubes in a coupled fluidized bed, the process is as follows figure 2 As shown, the specific steps are as follows:
[0027] The method consists of two parts: catalyst reduction activation and carbonization reaction, wherein the catalyst reduction activation reactor 101 is a conventional fluidized bed reactor, and the upper part 1011 of the catalyst reduction activation reactor 101 is made of a metal material with good thermal conductivity, and the lower half Section 1012 is made of stainless steel powder sintered material capable of filtering. The fluidized bed carbonization reactor 104 is composed of three parts, including a top settling section 1041 , a middle circulation fluidized bed reactor 1042 , and a lower fluidized bed collector 1043 . The catalyst reduction and activation reactor 101 is placed in the carbon nanotube reactor 104 , specifically in the top settling section 104...
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