Acetylene and carbon nanotube preparing plant
A technology of carbon nanotubes and acetylene, applied in a device for preparing acetylene and carbon nanotubes, in the field of devices for preparing acetylene and carbon nanotubes, can solve the problems of low catalyst utilization efficiency, complicated process, and low thermal efficiency, and achieve structural Simple and scientific, easy to operate, and the effect of improving utilization efficiency
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Embodiment approach 1
[0018] First connect the plasma generator 1, the feed mixer 2, the descending reactor 3, the separation collector 4, and the powder feeder 5 in order from top to bottom, and the powder feeder 5 passes through the powder supply pipeline and the feed mixer 2 connect. The plasma generator 1 is placed above the descending reactor 3 , and the arc jet generated by the plasma generator 1 passes through the central channel of the feed mixer 2 and extends into the descending reactor 3 . The diameter of the annular cooling channel 202 inner central channel of the feed mixer 2 is 15 millimeters, and the nozzle 201 passes the outer wall of the cooling channel 202, passes through the cooling channel area, passes through the inner wall of the cooling channel 202, communicates with the central channel, and the nozzle 201 The angle of inclination is zero degrees (such as figure 2 -A shown). The inner diameter of the descending reactor 3 is 15 mm, and the height is 350 mm. The reactor wall ...
Embodiment approach 2
[0020] Other parts are the same as embodiment 1, in addition, the diameter of the inner central channel of the annular cooling channel 202 of the feed mixer 2 is 35 millimeters, and the angle of inclination of the nozzle 201 is 45 degrees (as figure 2 -B shown), the inner diameter of the descending reactor 3 is 35 mm, the height is 800 mm, and the diameter of the delivery pipe 511 is 10 mm.
Embodiment approach 3
[0022] Other parts are the same as embodiment 1, in addition, the diameter of the inner central channel of the annular cooling channel 202 of feed mixer 2 is 20 millimeters, and the angle of inclination of nozzle 201 is-45 degree (as figure 2 -C shown), the inner diameter of the descending reactor 3 is 20 mm, the height is 600 mm, and the diameter of the delivery pipe 511 is 8 mm.
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