microsecond time-scale), and a high gas pressure (tens of MPa)
is produced. Under such conditions, the instant density of
carbon species inside the reactor is very high, about 0.009 mol
cm23 carbon atoms, while the tube growth is very effective so
that 80–90% tube content is available. This means that the CNT
growth rate is extremely high, in accord with the theoretical
estimation: a multi-wall CNT with 5 nm diameter and 1000 mm
length grows in 1023–1024s.10 On the other hand, the
fluctuating system temperature and the high density of carbon
species are perhaps responsible for the formation of the
structural defects. The introduction of paraffin increases the
number of defects, especially for high paraffin–PA ratios.
Our synthesis of CNTs by a detonation process is certainly
not the first. Kroke et al.11 recently observed CNTs being
formed after a detonation of 2,4,6-triazido-s-triazine (C3N12),
although they employed a specially prepared explosive with
very low carbon content and operated at a high CJ pressure
(1.63 GPa), which resulted in a very low content of CNTs of
only 2%.
In our approach, a very common CHNO explosive, PA, is
employed, a catalyst and additional hydrocarbon are introduced
into the detonation system, and the detonation occurs at very
low CJ density and pressure. Such a detonation process is
chemically much different from that for pure C/N explosives
and undoubtedly facilitates practical operation. On the other
hand, compared to the other processes for CNT syntheses, our
process is characterized by high-density and high-pressure
conditions, which experimentally shows that CNTs can grow in
such an environment and provides an alternative process for
CNT synthesis and a new route for theoretical studies on tubule
growth, especially in high density environments and in the
presence of metal catalysts.
Fig. 1 SEM (A) and TEM (B) images of a typical product from the
detonation of a PA–Co(Ac)2–paraffin mixture, showing that tubular
structures are dominant. Inset of B shows one tubule capped by a cobalt
particle.
Notes and references
† The employed paraffin has a boiling point of 300 °C and carbon and
hydrogen content of 82 wt% and 18 wt%, respectively.
‡ SEM and TEM analyses were carried out at a scanning electron
microscope (Philips XL30-FEG) and transmission electron microscope
(Philips CM200-FEG), respectively.
constructed by several to tens graphite layers parallel to the tube
axis, with an interlayer spacing of 0.34 nm as revealed by high-
resolution TEM (Fig. 2), but some of them have obvious defects
in the graphite networks. Cobalt nanoparticles are frequently
located at the ends of the CNTs, with sizes close to the diameters
of the tubes (inset of Fig. 1B), suggesting that the CNT growth
mechanism in the present process is similar to that in the
catalytic decomposition of hydrocarbons,9 in which the tubules
grow by the extrusion of carbon, dissolved in a metallic catalyst
particle that is over-saturated in carbon at one part of the
surface.
However, there are large differences between the present
detonation process and the traditional catalytic decomposition
of hydrocarbons or CO. In our process, the system temperature
is generated by the exothermic decomposition of explosive
following a self-heating process and drops quickly after the
detonation.§ Additionally, all carbon species for CNT assem-
bling are supplied in an extremely short period (on a
§ During experiments, we stop heating while the detonation occurs and
place the reactor in air for cooling.
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Fig. 2 High-resolution TEM image showing that the tube walls are well
crystallized.
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