rate to diffusive mass transfer rate and is given by uL/D,
where u is a characteristic flow velocity, L a characteristic
length scale, and D the diffusion coefficient. L is 5 mm and
D is estimated to be 1300 cm2/s ͑at 1000 °C, 5 Torr͒. The
Peclet number is calculated to be on the order of 10, indicat-
ing that convection, instead of diffusion ͑as in a hot-filament
CVD͒, is the dominant mechanism of mass transport. The
residence time in the hot-tube system is 25 s, which is
much smaller than the residence time of 2ϫ103s for the gas
to diffuse from the filament to substrate in a typical hot-
filament CVD at 20 Torr.14 Furthermore, the outer graphite
tube temperature was around 1000 °C, much lower than the
filament temperature in a hot-filament CVD, indicating a
much lower average gas temperature in the hot-tube system.
Owing to the lower gas temperature and much shorter resi-
dence time, the extent of gas phase reaction in the hot-tube
system is far less than that in a conventional hot-filament
CVD, resulting in the gaseous carbon species near the sub-
strate surface possessing the characteristic structure of the
input carbon source.
conditions. Martin and Hill3 have shown that the efficiency
of diamond growth from the CH3 radical is about ten times
higher than that for C2H2; however, their film produced from
C2H2 contains a much smaller fraction of diamond phase
than that from CH4.15 Besides, we do not observe the dia-
mond growth from C2H2 on diamond crystallite seeds as re-
ported by Martin.6 More results will be published soon. Our
results tend to be consistent with those by Lee et al.5
In conclusion, due to the small residence time and low
gas temperature in the hot-tube system, the CH4–C2H2 inter-
conversion is insignificant so almost pure CH4 or C2H2 near
the substrate surface can be obtained. Diamond can be syn-
thesized relatively fast with the CH4 dominant carbon spe-
cies near the growth surface; however, diamond growth is
negligible with the C2H2 dominant carbon species near the
growth surface. Under the Cl-rich conditions, the CH3 radi-
cal seems the only diamond growth precursor whereas
C2H2 is inefficient to grow diamond.
The financial support of this work, by the National Sci-
ence Council of the Republic of China under Contract No.
NSC-82-0405-E-006-479, is gratefully acknowledged.
In order to identify the diamond growth precursor, the
conditions under which the carbon species was almost pure
CH4 or C2H2 ͓rows ͑b͒ and ͑c͒, respectively, in Table I͔ were
employed to grow diamond. With 0.3% CH4 being the input
carbon source, an almost continuous diamond film was de-
posited after 2 h growth, as shown in Fig. 2͑a͒. The Raman
spectrum of the deposit in Fig. 2͑a͒ is shown in Fig. 3, and
the 1332 cmϪ1 peak confirms the formation of diamond. On
the other hand, with 0.15% C2H2 being the input carbon
source, only a few very small particles were deposited, as
demonstrated from the very small bright spots in Fig. 2͑b͒.
The above results are very reproducible. The deposition rate
with almost pure C2H2 is negligible compared to that for
almost pure CH4. Since CH4 is less likely to be the diamond
growth precursor, the CH3 radical formed by
CH4ϩH→CH3ϩH2 or CH4ϩCl→CH3ϩHCl should be the
diamond growth precursor as proposed by Harris.1 There-
fore, we conclude that the CH3 radical seems the only dia-
mond growth precursor whereas C2H2 is not under the above
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11 J.-J. Wu and F. C.-N. Hong ͑unpublished͒.
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129.120.242.61 On: Wed, 26 Nov 2014 11:32:42