Method and device for mass growth of high-quality, straight carbon nanotubes in low-temperature gas phase
A carbon nanotube, high-quality technology, applied in the field of carbon nanotube preparation, can solve problems such as uneven diameter of carbon nanotubes, unstable catalyst supply, excess catalyst supply, etc., achieve good industrialization prospects, uniform diameter and reliable The effect of control and low usage
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Embodiment 1
[0039] device such as figure 1 As shown, catalyst precursor (ferrocene powder), growth promoter (sulfur powder), porous silica powder (average particle size is 100nm, average pore diameter is 7nm, porosity 35%) by weight ratio 100:1:1000 The ratio is mixed evenly and placed in the reaction device figure 1 in the programmed temperature heating pack. The flow rate in the reaction zone is 10ml / cm 2 Raise the temperature to 1000 °C under the protection of hydrogen for min, raise the temperature-controlled heating bag with the catalyst precursor to 40 °C, and feed the carbon source trichlorobenzene (8×10 -5 Gram equivalent carbon / min·cm 2 ) and carrier gas hydrogen (20ml / cm 2 min), increase the hydrogen flow directly into the reactor to 15ml / cm 2 min, carbon nanotubes start to grow, and the growth time is 20 min. In this embodiment, the supply amount of the catalyst precursor is 2×10 -8 Gram equivalent / hour·cm 2 , the supply of growth promoter is 2×10 -10 Gram equivalent / h...
Embodiment 2
[0042] device such as figure 1 As shown, catalyst precursor (ferrocene powder), growth promoter (sulfur powder), porous silica powder (average particle size is 10nm, average pore diameter is 2nm, porosity 50%) by weight ratio 100:1:1000 The ratio is mixed evenly and placed in the reaction device figure 1 in the programmed temperature heating pack. The flow rate in the reaction zone is 10ml / cm 2 Raise the temperature to 1000 °C under the protection of hydrogen for min, raise the temperature-controlled heating bag with the catalyst precursor to 30 °C, and feed the carbon source methane (1×10 -5 Gram equivalent carbon / min·cm 2 ) and the carrier gas hydrogen (5ml / cm 2 ·min), through the etchant water vapor (6×10 -6 Gram equivalent water / min·cm 2 , the free radicals are hydrogen and hydroxyl radicals), and the hydrogen flow directly into the reactor is increased to 15ml / cm 2 ·min, carbon nanotubes start to grow, and the growth time is 40min. In this embodiment, the supply a...
Embodiment 3
[0045] The device adopts a vertical reaction furnace, catalyst precursor (nickelocene powder), growth promoter (thiophene), porous magnesium oxide powder (average particle size 500nm, average pore diameter 80nm, porosity 80%) in a weight ratio of 100:1 : 1000% mixed evenly, placed in the reaction device figure 1 in the programmed temperature heating pack. The flow rate in the reaction zone is 10ml / cm 2 Under the protection of hydrogen for min, the temperature was raised to 600°C, and the programmed temperature control heating bag with the catalyst precursor was raised to 30°C, and the carbon source ethanol (2×10 -4 Gram equivalent carbon / min·cm 2 ) and the carrier gas hydrogen (5ml / cm 2 min), increase the hydrogen flow directly into the reactor to 15ml / cm 2 ·min, carbon nanotubes start to grow, and the growth time is 40min. In this embodiment, the supply amount of the catalyst precursor is 2×10 -8 Gram equivalent / hour·cm 2 , the supply of growth promoter is 2×10 -10 Gr...
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Abstract
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