Solid carbon nanoparticles are promising growth seeds to prepare single-walled carbon nanotubes (SWCNTs) at high temperatures, at which the SWCNT crystallinity should be improved significantly but conventional metal catalyst nanoparticles are unstable and suffer from aggregation. The noncatalytic nature of solid carbon nanoparticles, however, makes SWCNT growth inefficient, resulting in a limited growth yield. In this study, we develop a two-step chemical vapor deposition process to efficiently synthesize high-crystallinity SWCNTs at high temperatures from solid carbon nanoparticles obtained from nanodiamond. Based on thermodynamic considerations, the growth conditions are separately adjusted to supply different growth driving forces which are suitable for the formation of the initial cap structures and for the stationary elongation of SWCNTs. This process, called cap formation engineering, improves the nucleation density of the cap structures. We examined the changes in crystallinity, amorphous carbon deposition, diameter, and yield of SWCNTs with respect to the synthesis conditions. By controlling the initial growth conditions, high-quality SWCNTs are grown with improved yield. With the addition of water vapor as the etchant, deposition of amorphous carbon at high temperatures was further prevented. The results provide a pathway for precise growth control of SWCNTs from unconventional solid growth seeds.
Solid carbon nanoparticles are promising growth seeds to prepare single-walled carbon nanotubes (SWCNTs) at high temperatures, at which the SWCNT crystallinity should be improved significantly but conventional metal catalyst nanoparticles are unstable and suffer from aggregation. The noncatalytic nature of solid carbon nanoparticles, however, makes SWCNT growth inefficient, resulting in a limited growth yield. In this study, we develop a two-step chemical vapor deposition process to efficiently synthesize high-crystallinity SWCNTs at high temperatures from solid carbon nanoparticles obtained from nanodiamond. Based on thermodynamic considerations, the growth conditions are separately adjusted to supply different growth driving forces which are suitable for the formation of the initial cap structures and for the stationary elongation of SWCNTs. This process, called cap formation engineering, improves the nucleation density of the cap structures. We examined the changes in crystallinity, amorphous carbon deposition, diameter, and yield of SWCNTs with respect to the synthesis conditions. By controlling the initial growth conditions, high-quality SWCNTs are grown with improved yield. With the addition of water vapor as the etchant, deposition of amorphous carbon at high temperatures was further prevented. The results provide a pathway for precise growth control of SWCNTs from unconventional solid growth seeds.
Carbon
nanotubes (CNTs),[1] which are
a quasi-one-dimensional nanomaterials whose structures are formed
by seamlessly rolling up single-layer or multilayer graphene sheets,
offer diverse excellent properties and are promising for mechanical,[2] electronic,[3] and thermal
applications.[4] Especially, single-walled
CNTs (SWCNTs)[5] have received increasing
attention toward logic circuits,[6] chemical
sensors,[7] and quantum light sources[8] due to their superior performances and chirality-dependent
optoelectronic properties.[9] Various methods
have been developed to obtain SWCNTs. Examples include arc discharge,[10] laser ablation,[11] and chemical vapor deposition (CVD).[12] In such growth processes, carbon atoms decomposed from carbon source
molecules are bonded together on a suitable growth seed, which is
a nanoparticle acting as a template, to initially form a hemispherical
graphitic structure, which is called a cap structure. After the lift-off
of the cap structure from the growth seed, a tube structure gradually
elongates with the attachment of carbon atoms at the interface of
the tube edge and the growth seed.[13] Due
to the high degree of freedom of the growth parameters and the excellent
compatibility with large-scale production, the CVD process has been
extensively studied to realize structure-controlled and high-yield
synthesis of SWCNTs.[14−17]Unfortunately, large discrepancies remain between experimentally
synthesized SWCNTs and ideal SWCNTs, which are required for applications
in terms of crystallinity, chirality, length, etc. The crystallinity
of SWCNTs is one of the most important aspects because structural
defects formed on SWCNTs drastically change the electronic structure[18,19] and deteriorate their superior properties, including electrical
transport,[18,20,21] thermal transport,[22] and mechanical strength.[23] To achieve highly crystalline SWCNTs, high-temperature
CVD processes are effective because the activation barrier for healing
defects must be overcome.[24,25] For high growth temperature,
growth seeds for SWCNTs require high temperature stability to prevent
aggregation phenomena. Catalytic metal nanoparticles, including iron,[26,27] nickel,[28] cobalt,[29] and relevant alloys,[30] are widely
used as growth seeds. However, they suffer from deactivation induced
by aggregation due to their moderate melting points, limiting the
yield of SWCNTs at high temperature.[31] At
the same time, the post-treatment step to exclude metal impurities
from as-grown SWCNTs is needed for some applications, but it induces
the formation of additional defects.[32]Recently, nonmetallic nanoparticles with higher melting points
have been utilized as growth seeds of SWCNTs.[33−37] Among them, nanodiamond (ND)[38] is a promising growth seed due to its nonfusion characteristic,
which prevents aggregation or sintering of nanoparticles even at high
growth temperatures. In addition, as-grown SWCNTs from ND nanoparticles
are highly pure in terms of elemental composition, mitigating the
need for postgrowth purification. One study successfully synthesized
highly crystalline SWCNTs at 1000 °C using solid carbon nanoparticles
derived from NDs as growth seeds.[39] However,
the yield of high-quality SWCNTs is still low at high growth temperatures.
It has been reported that increasing the growth temperature makes
it more difficult to organize SWCNTs.[39]The change in the growth efficiency as a function of temperature
can be explained by thermodynamic considerations. The growth driving
force Δμ is the difference between the chemical potential
μ of carbon atoms in carbon feedstock molecules in the gas phase
μC(gas) and that of carbon atoms in SWCNTs in the
solid phase μC(solid), which is expressed as Δμ
= μC(gas) – μC(solid) (Figure S3). Both the growth temperature and the
carbon source partial pressure affect Δμ.[40] Since μ is equal to the partial molar Gibbs energy,
when pressure p is kept constant and temperature T is changed, the variation of μ is proportional to
the partial molar entropy Sm according
to the equation . Because Sm in the gas phase is higher than that in the
solid phase and μC(gas) decreases more drastically
than μC(solid) as the growth temperature increases,
these result in a reduction
of Δμ at higher temperatures (Figure S3c). Such a decrease in Δμ at high temperatures
makes the formation of SWCNTs difficult, especially for cap structures
with a higher strain energy, which exceeds μC(solid).[24] As another influential factor, the
change in the carbon source partial pressure mainly affects μC(gas). A higher carbon source partial pressure increases μC(gas), which increases Δμ (Figure S3d).Since SWCNT growth begins with the cap
formation process, optimizing
the cap formation condition for a higher nucleation efficiency is
necessary to increase the SWCNT growth yield. Thus, an increase in
the partial pressure of the carbon feedstock or a decrease in the
growth temperature only at the beginning of SWCNT growth should compensate
for the high driving force required for cap structure nucleation.
After the efficient formation of the cap structures, a moderate driving
force should be supplied for subsequent growth of the nanotube sidewalls
by controlling the growth condition. The details of driving force
required for the different growth stages will be explained in Section . A two-step
growth approach has been employed in SWCNT synthesis using conventional
metal nanoparticles at a moderate temperature.[41] However, so far, the effectiveness of two-step growth has
scarcely been investigated for a solid seed-supported growth system
of SWCNTs, where a unique vapor–solid surface–solid
(VSSS) growth mechanism[37,38] takes place rather
than vapor–liquid–solid (VLS) model[42,43] employed for metal catalyst-based growth. Although our previous
study reported a preliminary result on two-step growth from solid
carbon seeds by temporally changing the carbon feeding rate,[44] a more thorough investigation on the cap formation
process should realize an efficient synthesis of high-crystallinity
SWCNTs and shed light on the unconventional growth mechanism of SWCNTs
from solid carbon nanoparticles.Another factor that prevents
the growth of SWCNTs is the deposition
of amorphous carbon (a-C), which tends to form under the conditions
of high temperature and high carbon feeding rates. In metal catalyst-based
CNT growth, with the introduction of water vapor, it has been reported
that the activity and lifetime of the metal catalyst were enhanced
by selective etching of a-C. The improvement of catalyst property
during growth enables a highly efficient synthesis of CNTs and results
in massive or superlong CNT growth from metal nanoparticles.[15,45−49] Thus, water-induced etching of a-C has the potential to be utilized
in the growth of SWCNTs from solid carbon seeds.In this work,
a two-step approach is developed to efficiently synthesize
high-quality SWCNTs using ND-based solid carbon nanoparticles as growth
seeds at high temperatures. The effects of growth temperature, carbon
feedstock partial pressure, and growth time during the initial growth
step on the nucleation of SWCNT caps are investigated to enhance the
synthesis from nonmetallic nanoparticles. Following the highly efficient
cap formation stage, the carbon supply is reduced to adjust the growth
driving force during the secondary growth step at a high temperature.
Stationary elongation of tubes in the secondary growth step increases
the growth yield of SWCNTs with high crystallinity. Furthermore, highly
crystalline impurity-free SWCNTs are obtained with an improved growth
yield by introducing water vapor as an etchant just after the formation
of the SWCNT cap structures.
Experimental Section
Growth Seed Preparation
Figure depicts the whole
process, including the pretreatment step of growth seeds and the two-step
growth process with and without using water. Purified ND particles
(impurity concentrations of 80 ppm for Fe, 2100 ppm for Zr, and 6–20
ppm for Pd) prepared by the detonation method[50,51] were dispersed in ethanol (2.0 wt %) and used as the starting material
of the seeds for SWCNT growth. It should be noted that we performed
a separate experiment and confirmed that SWCNTs were grown not from
metal impurity contained in purified ND but from solid carbon nanoparticles
which were transformed from ND (Figure S1).
Figure 1
(a) Schematic diagram of the growth seed pretreatment and the two-step
growth process of SWCNTs from solid carbon nanoparticles. (b) Temperature
profile of the reaction furnace as a function of processing time.
(a) Schematic diagram of the growth seed pretreatment and the two-step
growth process of SWCNTs from solid carbon nanoparticles. (b) Temperature
profile of the reaction furnace as a function of processing time.Si substrates with a 300 nm thick thermal oxide
layer were cut
into an ∼10 mm square and cleaned by an ozone treatment process
(L-UV253, Japan Electronics Industry) by flowing 6 L/min oxygen for
5 min under ultraviolet light for 60 min followed by exhausting with
6 L/min nitrogen for 5 min. After ultrasonic dispersion, 20 μL
of the ND solution was dropped on the surface of the Si substrates.
Additionally, the same Si substrates without any growth seeds were
used as a reference to examine the amount of a-C deposited directly
on substrates (hereafter called blank samples).
Two-Step Growth Process without Water Vapor
Injection
A tubular CVD furnace (GE-1000, GII Techno) was
used for pretreatment of the growth seeds and the synthesis of SWCNTs.
After the substrate was placed at the center of the quartz tube chamber
which had a semicircle cross section with a diameter of 43.6 mm and
whose heating zone length is 890 mm, the surface cleaning process
was held while heating in air for 10 min at 600 °C to remove
various impurities on the substrate and the surface of ND (Figure b, process 1). During
this process, the diameter of ND was reduced to the appropriate size
for SWCNT growth,[38] and the size variation
is presented in Figure S2. Further treatment
was followed by gradually increasing the furnace temperature to 1000
°C and keeping it at 1000 °C for 1 h as an annealing procedure
under the condition of Ar at 85 kPa (Figure b, process 2). This step should change the
surface of ND (sp3 carbon) into a more stable graphitic
shell (sp2 carbon), which is called the carbon nano-onion
structure.[52,53]To adjust the growth condition
suitable for the initial growth step, where the cap structures are
formed, the growth temperature was set to 850 or 900 °C after
the aforementioned annealing process at 1000 °C (Figure b, process 3). Once the temperature
dropped to the set value, which was determined based on the previous
high-temperature SWCNT synthesis condition,[39] the pressure was decreased to 500 Pa while continuously injecting
Ar at 20 sccm and kept for 3 min for environment stabilization. After
that, the gas condition was switched to a 20 sccm mass flow mixture
of C2H2 (2%)/Ar (1–10 sccm) and H2 (3%)/Ar (10–19 sccm), while the total pressure was
kept at 500 Pa, corresponding to a C2H2 partial
pressure of 0.5–5 Pa. The typical flow rates of C2H2/Ar and H2/Ar were 2 and 18 sccm, respectively,
corresponding to a C2H2 partial pressure of
1 Pa. The process lasted for 1 or 2 min as the cap growth stage. Before
moving into the secondary growth step, the growth temperature was
increased to 1000 °C while controlling the gas mixture to 1 sccm
C2H2 (2%)/Ar and 19 sccm of H2 (3%)/Ar,
where the partial pressure of C2H2 was 0.5 Pa
(Figure b, process
4). The secondary growth step, where stationary elongation of SWCNTs
should occur, began when the growth temperature reached 1000 °C
and continued for 30 min while keeping the same gas-phase mixture
and pressure conditions (Figure b, process 5). Under some experiments, only the initial
growth step was conducted, and the temperature was decreased after
the 1 or 2 min growth at 850 or 900 °C without the secondary
growth step.
Two-Step Growth Process
with Water Vapor Injection
Water vapor was added in some
experiments as a growth enhancer
because the vapor may prevent the deposition of a-C. Based on the
two-step growth process presented above, water vapor typically at
0.15 Pa was injected into the gas phase environment. We started supplying
water at two different timings: from the beginning of the temperature
rising step and from the beginning of the secondary growth step. The
details are explained in Section .
Structure Characterization
and Yield Evaluation
of Synthesized SWCNTs
We analyzed the structure of the synthesized
SWCNTs with Raman spectroscopy. A Raman spectrometer (LabRAM HR800,
HORIBA Jobin Yvon) was used with an excitation wavelength λex of 633 nm. The laser spot size was about 0.9 μm, and
the laser power was around 7 mW at the measurement point. The exposure
time of each measurement spot was 1 s for five cycles. Raman spectra
were collected from 30 randomly selected spots on each sample, and
the average spectra were used for further analysis. The quality of
formed SWCNTs was discussed by comparing the intensity ratio of the
G band (∼1590 cm–1) to the D band (1330–1360
cm–1), which was represented as IG/ID.[54] The density of SWCNTs was low, and the G band was occasionally not
observed in the high-temperature synthesis case. Thus, the growth
yield of SWCNTs was evaluated through the observation frequency of
the G band (the number of appearances of the G band in the measured
spectra divided by the total number of measurements). Typically, Raman
spectra of 100 spots were collected for the evaluation of the G band
observation frequency. Note that more measurement spots were used
to determine the G-band observation frequency than that for averaging
Raman spectra to ensure the accuracy of the G-band observation frequency
even for samples with low-density SWCNTs. Scanning electron microscopy
(SEM) (NVision, Carl Zeiss and S-4800, Hitachi) was used for morphology
observations of SWCNTs with an acceleration voltage of 1 kV.
Results and Discussion
Effects of Temperature
and C2H2 Partial Pressure in the Initial Growth
Step
To improve
the growth efficiency of cap structures from solid carbon nanoparticles
as growth seeds, SWCNT growth was performed under various initial
growth conditions while omitting the secondary growth step. To magnify
the difference of the growth results, the growth time of the initial
growth step was preliminarily set at 2 min. Figure presents the influence of the growth temperature
and the partial pressure of carbon feedstock during the initial growth
step.
Figure 2
Dependence of the initial growth conditions on the structure and
yield of SWCNTs. (a) Raman spectra of SWCNTs grown at 850 and 900
°C with C2H2 partial pressure of 1 Pa for
2 min. Dotted lines denote Raman spectra of the blank samples obtained
under the same conditions. (b) G band observation frequency of SWCNTs
synthesized at 850 and 900 °C with a carbon source partial pressure
of 0.5 and 1 Pa for 2 min, which represents the growth yield of SWCNTs.
(c) Raman spectra of SWCNTs grown at different carbon source partial
pressures: 0.5, 1, 2.5, and 5 Pa. The growth temperature is 850 °C,
and the growth time is 2 min. Inset shows magnified spectra. (d) Radial
breathing mode (RBM) peaks in Raman spectra of SWCNTs synthesized
through only the initial growth step of 850 °C, 1 Pa, and 2 min
(denoted as 850 °C 2 min) and 850 °C, 1 Pa, and 10 min (850
°C 10 min) as well as through the initial growth step of 850
°C, 1 Pa, and 2 min followed by the secondary growth step of
1000 °C, 0.5 Pa, and 30 min (850 °C 2 min–1000 °C
30 min). (e) Reaction coordinate and different growth driving force
for the cap formation (Δμ, solid line) and the stationary
elongation (Δμ′, dotted line) by only initial growth
step (fixed growth condition). (f) Schematic of growth driving force
variation for the cap formation and the stationary elongation with
different diameters by only initial growth step. (g) Reaction coordinate
and different growth driving force by the two-step growth. Growth
driving force for the cap formation in the initial growth step (Δμ,
solid line) and the stationary elongation in the secondary growth
step (Δμ′, dotted line) is shown. (h) Schematic
of growth driving force variation for the cap formation and the stationary
elongation with different diameters by the two-step growth.
Dependence of the initial growth conditions on the structure and
yield of SWCNTs. (a) Raman spectra of SWCNTs grown at 850 and 900
°C with C2H2 partial pressure of 1 Pa for
2 min. Dotted lines denote Raman spectra of the blank samples obtained
under the same conditions. (b) G band observation frequency of SWCNTs
synthesized at 850 and 900 °C with a carbon source partial pressure
of 0.5 and 1 Pa for 2 min, which represents the growth yield of SWCNTs.
(c) Raman spectra of SWCNTs grown at different carbon source partial
pressures: 0.5, 1, 2.5, and 5 Pa. The growth temperature is 850 °C,
and the growth time is 2 min. Inset shows magnified spectra. (d) Radial
breathing mode (RBM) peaks in Raman spectra of SWCNTs synthesized
through only the initial growth step of 850 °C, 1 Pa, and 2 min
(denoted as 850 °C 2 min) and 850 °C, 1 Pa, and 10 min (850
°C 10 min) as well as through the initial growth step of 850
°C, 1 Pa, and 2 min followed by the secondary growth step of
1000 °C, 0.5 Pa, and 30 min (850 °C 2 min–1000 °C
30 min). (e) Reaction coordinate and different growth driving force
for the cap formation (Δμ, solid line) and the stationary
elongation (Δμ′, dotted line) by only initial growth
step (fixed growth condition). (f) Schematic of growth driving force
variation for the cap formation and the stationary elongation with
different diameters by only initial growth step. (g) Reaction coordinate
and different growth driving force by the two-step growth. Growth
driving force for the cap formation in the initial growth step (Δμ,
solid line) and the stationary elongation in the secondary growth
step (Δμ′, dotted line) is shown. (h) Schematic
of growth driving force variation for the cap formation and the stationary
elongation with different diameters by the two-step growth.The Raman spectra in Figure a show the variations of the SWCNT growth
results only with
an initial growth step at temperatures of 850 and 900 °C. For
the same carbon source partial pressure (1 Pa) and growth time (2
min), the sample synthesized at 900 °C shows a higher intensity
of the G band than that synthesized at 850 °C. Since the G band
intensity reflects the amount of SWCNTs in the measurement area, its
increase indicates that the initial growth efficiency of SWCNTs improves
as the temperature increases from 850 to 900 °C. The D band peaks,
which originate from structural defects formed on SWCNTs and/or a-C
deposited on the surface of SWCNTs and substrates, are observed in
both samples. On the other hand, the D band peaks are not observed
from the control samples without ND deposition (blank samples, Figure a, dotted lines).
The absence of the D band from the blank samples suggests that the
D band of the SWCNT samples is mostly rooted in defects formed on
SWCNTs instead of a-C, which can also be deposited on blank samples.
The higher G band and D band intensity from the sample synthesized
at 900 °C implies that stationary growth of SWCNTs may begin
with a higher growth efficiency even in the initial growth step. The
earlier start of stationary growth may be responsible for the quality
degradation of SWCNTs obtained at 900 °C, which will be discussed
in Section .The influences of the growth temperature and the carbon source
partial pressure on the growth yield of SWCNTs were examined by recording
the G band observation frequencies of the samples grown at 850 and
900 °C and at 0.5 and 1 Pa, as shown in Figure b. The increase in the growth temperature
from 850 to 900 °C results in an obvious improvement in the growth
yield. It should be noted that the yield of SWCNTs grown at 900 °C
decreases when the partial pressure of C2H2 is
slightly increased from 0.5 to 1 Pa. The decrease in the growth efficiency
as the carbon supply increases at high temperatures may be related
to the deposition of a-C around the growth seeds. Because the growth
seed nanoparticles should possess a high surface energy compared with
flat SiO2/Si substrate, a-C is more easily adsorbed on
SWCNT growth samples with growth seeds than blank samples. This explains
why almost no D band appears on the blank samples but a small amount
of a-C is deposited on the SWCNT samples (Figure a, dotted line). At the higher temperature
for cap formation, the increase of carbon source partial pressure
helps to enhance the growth driving force, which makes it easier to
overcome the activation barrier for the nucleation of SWCNT caps.
Since a higher growth driving force also makes it easier to meet the
growth threshold of a-C, a higher temperature accelerates the deposition
of a-C. The faster formation rate of a-C on the growth surface lowers
the growth efficiency of the cap structure and hinders its lift-off
from the nanoparticle. In the case of growth at higher temperatures
above 900 °C, the increase of the carbon source partial pressure
enhances the deposition rate of a-C on the surface of the growth seeds.
Thus, part of the growth seeds is deactivated ahead of time even when
the initial growth is not finished, which results in a decrease in
the growth yield.The effect of the carbon source partial pressure
in the initial
growth step was examined over a wider range from 0.5 to 5 Pa at 850
°C for 2 min. Figure c shows the Raman spectra of the samples. The weak G band
intensity observed for the samples grown with C2H2 partial pressures of 0.5 and 1 Pa indicates that the initial nucleation
of SWCNT caps already occurs but few SWCNTs move into the next growth
stage in which nanotubes elongate stationarily. When the partial pressure
of C2H2 is increased to 2.5 or 5 Pa, the G band
and D band intensities obviously increase. Cap structures of SWCNTs,
which are a hemispherical carbon cage similar to half of a C60 molecule, are expected to exhibit no detectable Raman signals in
the same wavenumber region as the G and D bands.[55] Therefore, the stronger G and D band intensity indicates
that most of SWCNTs have already entered into the stationary elongation
stage in the case of 2.5 or 5 Pa. Unlike the growth at 900 °C,
the surface of the growth seeds remains clean at a slower a-C deposition
rate of 850 °C, which allows for enough time to finish the nucleation
procedure (Figure a). In the meantime, the increased carbon source partial pressure
oversupplies carbon atoms to the growth seeds during the initial growth
step, which results in the early start of stationary growth even at
the lower growth temperature and the formation of defective SWCNTs
(Figure c, 2.5 and
5 Pa).The experimental results for the growth temperature and
the carbon
source partial pressure suggest that the initial growth step should
be well controlled to achieve a high nucleation efficiency of cap
structures and, at the same time, further stationary growth of SWCNTs
should be avoided during this step. Thus, the initial growth process
conducted at 850 °C with 1 Pa C2H2 is suitable
for further yield improvements of high-quality SWCNTs and is employed
in the later experiments. It should be noted that the solid carbon
nanoparticles employed as growth seeds in this study do not possess
a high catalytic activity, which largely differs from conventional
metal catalysts. Hence, the carbon feedstock concentration has to
be controlled with high precision to realize efficient SWCNT growth,
especially in the cap nucleation stage.
Two-Step
Growth of SWCNTs and Diameter Variations
In the SWCNT growth
process, the diameter of SWCNTs is determined
mainly by the formed cap structure. Therefore, different nucleation
rates of SWCNTs with various diameters were studied indirectly by
characterizing the SWCNT tube diameter through radial breathing modes
(RBMs) in the Raman spectra (Figure d). Samples were synthesized only with the initial
growth step at 850 °C for 2 or 10 min. A sample grown with the
secondary growth step at 1000 °C for 30 min after initial growth
at 850 °C for 2 min was also examined. Comparison of the samples
synthesized at 850 °C for 2 and 10 min indicates that the RBM
peaks mainly appear at ∼130, ∼180, and ∼270 cm–1 in the 10 min case but the RBM peak appears only
at ∼130 cm–1 in the 2 min case. This difference
represents the growth behavior of SWCNTs as a function of diameter.
The thicker SWCNTs, which show the RBM peak at 130 cm–1, finish their nucleation and gradually enter into stationary growth
in the first 2 min.The diameter dependence of cap nucleation
can be explained well by the regulation of Δμ, the difference
between μC(gas) and μC(solid). The
variation of μC(gas) and μC(solid) is related to growth conditions such as temperature and carbon source
partial pressure. Besides, the thermodynamic parameters need to be
adjusted for different crystal structures of SWCNTs, such as the cap
structures and the tube structures with different diameters, which
own different strain energy. As reported previously,[24] in an actual reaction, reactants in the gas phase are not
in their standard state, and also strain energy should be considered.
Thus, at a constant temperature, the growth driving force for carbon
feedstock converting into an SWCNT (cap and tube) is expressed aswhere “°”, kB, d, and A/d2 represent the standard state, Boltzmann
constant,
diameter, and strain energy, respectively. The chemical potential
μC(solid) of SWCNT is influenced by the strain energy,
which depends on a part of the SWCNT (cap or tube structures) and
the diameter. The constant A differs depending on
the cap or the tube structure.Due to the higher strain energy,
the SWCNT cap structure presents
higher μC(solid) than the tube structure, which is
similar to the higher μC(solid) for thinner SWCNTs
than thicker SWCNTs. Therefore, under the same growth conditions (temperature
and partial pressure of C2H2), Δμ
for stationary elongation of the tube structure is higher than that
for cap formation and that for thicker SWCNT formation is higher than
that for thinner SWCNT formation (Figure S4). According to the above discussion, for the initial growth step,
Δμ provided by the growth condition must meet the threshold
of the driving force required for nucleation of the cap structures.
The initial growth step at 850 °C for 2 min represents a higher
growth efficiency for thicker SWCNTs, which have a higher Δμ
(Figure d, black line).
In the case of the only initial growth step, once the nucleation stage
is finished, the reduction of μC(solid) for the tube
increases Δμ for stationary elongation under the same
growth condition (Figure e). Such an increase makes Δμ fit the threshold
for elongation of thinner SWCNTs. On the other hand, this increase
can also result in a slight excess of Δμ for elongation
of thicker SWCNTs, which is above the growth window (Figure f). This leads to the increased
possibility of a-C formation, resulting in a decrease in the efficiency
of stationary elongation. This growth mechanism explains the result
of the stationary elongation stage after the cap formation stage only
with the initial growth step for the longer time (10 min), which shows
a delayed formation of thinner SWCNTs with RBM peak at ∼270
cm–1 and the appearance of stronger RBM peak at
∼180 cm–1 than that at ∼130 cm–1 (Figure d, red line). If we consider the two-step growth process,
after the initial growth, both the increase in the growth temperature
and the decrease in the carbon source partial pressure cause the decrease
of μC(gas) (Figure g). Additionally, μC(solid) also decreases
due to the structural change from a cap to a tube. These decreases
make Δμ for stationary elongation during the secondary
growth step similar to or lower than that for cap formation during
the initial growth step (Figure h). Such variation of the growth driving force contributes
to the stronger RBM peak at ∼130 cm–1 and
almost no RBM peak at ∼270 cm–1 (Figure d, blue line).
Effect of Growth Time in the Initial Growth
Step
The growth behavior of SWCNTs was also studied by changing
the initial growth time. Figure a,b shows the Raman spectra of the samples synthesized
at 850 °C with the initial growth step of 1 and 2 min with and
without the secondary growth step of 30 min, respectively. In the
case of only initial growth, a small D band appears from the 2 min
sample, whereas the D band from the 1 min sample is negligible. Considering
that the blank sample does not show a D band (Figure a, black dotted line), a-C deposition does
not occur even with 2 min. These results indicate that the D-band
from the 2 min sample originates from the defects and that the formation
of defects begins after the initial growth of 1 min.
Figure 3
(a, b) Raman spectra
of SWCNTs grown with different initial growth
times of (a) 1 min and (b) 2 min at 850 °C and 1 Pa, with (blue
line) and without (black line) the secondary growth step at 1000 °C
and 0.5 Pa for 30 min. (c) G band observation frequency of the four
samples with (blue bar) and without (black bar) the secondary growth
step.
(a, b) Raman spectra
of SWCNTs grown with different initial growth
times of (a) 1 min and (b) 2 min at 850 °C and 1 Pa, with (blue
line) and without (black line) the secondary growth step at 1000 °C
and 0.5 Pa for 30 min. (c) G band observation frequency of the four
samples with (blue bar) and without (black bar) the secondary growth
step.Furthermore, the RBM peaks of
the samples synthesized with the
secondary growth step at a high temperature exhibit information on
the temporal evolution of SWCNTs with different diameters. By conducting
the secondary growth step after the initial growth step of 1 or 2
min, a stronger RBM peak around ∼180 cm–1 emerges, which represents the extra formation of thinner SWCNTs
(Figure a,b). Since
SWCNTs are grown from solid nanoparticles which keep stable morphology
at high temperature, diameters of SWCNTs are defined at the stage
of cap structure formation and should remain unchanged during the
later growth stage. Thus, such extra formation of thinner SWCNTs reflects
that the higher amount of smaller size cap structures is formed while
prolonging initial growth time. Compared with the 1 min initial growth,
the higher RBM peak intensity at ∼180 cm–1 for the 2 min initial growth indicates a delay in thinner SWCNT
growth. The results confirm the diameter dependence of the nucleation
timing of SWCNTs in the cap formation stage, which was discussed in Figure d previously.Besides, the growth rate of SWCNTs with different thicknesses can
be discussed. As shown in Figure a,b, the RBM peak around ∼130 cm–1 appears in 1 and 2 min initial growth step when there is no thinner
SWCNT formed. This growth delay indicates the slower growth rate of
thinner SWCNTs than that of thicker SWCNTs from carbon solid nanoparticles.The growth yield variation upon adjusting initial growth time is
displayed in Figure c. Compared with the 1 min initial growth, a smaller increase in
the G band observation frequency before and after the secondary growth
step is observed for the initial growth of 2 min. This is presumably
because the initial growth of SWCNTs for 2 min induces some deposition
of a-C around ND particles, reducing the growth efficiency in the
subsequent growth step.
Water Vapor Injection during
Two-Step Growth
As the growth temperature increases, it becomes
more difficult
to avoid the formation of a-C on the surface of growth seeds just
by adjusting the supply rate of carbon feedstock. To prevent the deposition
of a-C, water vapor[15,46] was used to eliminate such deposition
via an oxidization reaction. The etching result was analyzed while
controlling the injection time and partial pressure of water vapor.
As schematically shown in Figure a, the etchant injection time was divided into three
cases: the addition of water vapor at the beginning of the initial
growth step (Figure a, process 1), the addition of the etchant at the beginning of the
temperature rising step (process 2), and the water vapor addition
at the beginning of the secondary growth step (process 3). Additionally,
the etchant concentration was separately controlled during the temperature
rising step and the secondary growth step. Here, samples are named
according to the three values of the water vapor pressure for processes
1, 2, and 3. For example, a sample grown without water vapor during
processes 1 and 2 and with the addition of water vapor at 0.15 Pa
during process 3 is represented by 0–0–0.15 Pa. As for
the other growth parameters, the optimized conditions in the previous
section were employed for the initial growth strep (850 °C with
1 Pa C2H2 for 1 min) and the secondary growth
step (1000 °C with 0.5 Pa C2H2 for 30 min).
Figure 4
(a) Profiles
of temperature and water vapor partial pressure for
the SWCNT two-step growth process with water vapor injection. (b)
Raman spectra of SWCNTs grown with different timings of water vapor
supply: without water vapor throughout the processes (0–0–0
Pa), without water vapor during the temperature rising step and supplying
it during the secondary growth step at 0.15 Pa (0–0–0.15
Pa), supplying water vapor both during the temperature rising step
and the secondary growth step at 0.15 Pa (0–0.15–0.15
Pa), and supplying water vapor during the whole process at 0.15 Pa
(0.15–0.15–0.15 Pa). Growth temperature, partial pressure
of C2H2, and growth time for the initial growth
step are fixed at 850 °C, 1 Pa, and 1 min, respectively, while
those for the secondary growth step are 1000 °C, 0.5 Pa, and
30 min, respectively. Dotted lines denote Raman spectra of the blank
samples. (c) G band observation frequency and IG/ID ratio of the same samples
as (b), which reflect the SWCNT yield and quality, respectively. Standard
deviation was also calculated and presented as the error bar of averaged IG/ID. (d) Raman
spectra of SWCNTs grown with different partial pressures of water
vapor for both the temperature rising step and the secondary growth
step. Dotted lines denote Raman spectra of blank samples. (e) Corresponding
G band observation frequency and IG/ID, which reflect the SWCNT yield and quality,
respectively. Standard deviation was also calculated and presented
as the error bar of averaged IG/ID.
(a) Profiles
of temperature and water vapor partial pressure for
the SWCNT two-step growth process with water vapor injection. (b)
Raman spectra of SWCNTs grown with different timings of water vapor
supply: without water vapor throughout the processes (0–0–0
Pa), without water vapor during the temperature rising step and supplying
it during the secondary growth step at 0.15 Pa (0–0–0.15
Pa), supplying water vapor both during the temperature rising step
and the secondary growth step at 0.15 Pa (0–0.15–0.15
Pa), and supplying water vapor during the whole process at 0.15 Pa
(0.15–0.15–0.15 Pa). Growth temperature, partial pressure
of C2H2, and growth time for the initial growth
step are fixed at 850 °C, 1 Pa, and 1 min, respectively, while
those for the secondary growth step are 1000 °C, 0.5 Pa, and
30 min, respectively. Dotted lines denote Raman spectra of the blank
samples. (c) G band observation frequency and IG/ID ratio of the same samples
as (b), which reflect the SWCNT yield and quality, respectively. Standard
deviation was also calculated and presented as the error bar of averaged IG/ID. (d) Raman
spectra of SWCNTs grown with different partial pressures of water
vapor for both the temperature rising step and the secondary growth
step. Dotted lines denote Raman spectra of blank samples. (e) Corresponding
G band observation frequency and IG/ID, which reflect the SWCNT yield and quality,
respectively. Standard deviation was also calculated and presented
as the error bar of averaged IG/ID.The decrease in the D
band intensity with the injection of etchant
demonstrates that water vapor helps prevent the formation of a-C,
although the timing of water vapor injection affects the quality (IG/ID ratio in Figure b) and quantity (G
band observation frequency in Figure c) of SWCNTs. Compared with the case in which water
vapor is injected from the secondary growth step (0–0–0.15
Pa), the case in which the injection time is set at the beginning
of the temperature rising step (0–0.15–0.15 Pa) exhibits
a higher purity of SWCNTs with a smaller a-C deposition, as indicated
by the lower D band intensity. It should be noted that the effect
of the water vapor concentration was separately examined for the case
of water vapor injection from the secondary growth step (Figure S5). As Figure S5 shows, even when varying the concentration, water vapor cannot etch
all of the deposited a-C. a-C may be partly formed before the water
vapor injection time during the period where temperature rises to
1000 °C.Water vapor was also injected from the beginning
of the initial
growth step (0.15–0.15–0.15 Pa). Compared with water
vapor injection from the end of the initial growth step, the case
where water vapor participated in the whole growth process exhibits
an obvious decrease in the growth yield according to the G band observation
frequency and the G band intensity. Such a reduction of the growth
yield reflects the negative effect of water vapor on SWCNT nucleation.
It has been reported that the cap of SWCNTs is more easily oxidized
and consequently destroyed than the sidewall due to the strain and
the pentagonal rings of the cap structure.[56] These results indicate that the starting time of etchant injection
should begin as soon as possible once the formation of cap structures
is finished when etchant is employed in a solid carbon seed-based
growth system to prevent a-C deposition and to enhance growth yield.The IG/ID ratio in Figure d and the G band observation frequency in Figure e show the effect of water vapor etching
as a function of partial pressures on the quality and quantity of
SWCNTs. While the partial pressure of water vapor during the temperature
rising step was fixed at 0.15 Pa, that during the secondary growth
step at 1000 °C was varied from 0 to 0.25 Pa. From 0 to 0.15
Pa (0–0.15–0, 0–0.15–0.1, and 0–0.15–0.15
Pa), both IG/ID and the G band observation frequency show a rising tendency with
the partial pressure, indicating efficient etching of a-C induced
by the participation of water vapor. On the other hand, increasing
the partial pressure to 0.2 Pa (0–0.15–0.2 Pa), even
though growth yield is further increased, the quality of SWCNTs decreases
considerably, and both the quality and the yield decrease when the
partial pressure continues to increase to 0.25 Pa (0–0.15–0.25
Pa). Since no obvious D band appears in the Raman spectra of the relevant
blank samples, the D band of the SWCNTs grown with water vapor of
0.2 and 0.25 Pa is attributed not to a-C but to the formation of structural
defects of SWCNTs. Similar to a previous study using metal nanoparticles,[57] this result suggests that an excess of water
vapor damages the SWCNT structures during the growth process but it
keeps the surface of growth seeds free from a-C and enhances the SWCNT
yield. In addition, as mentioned earlier, a further increase of SWCNT
yield appeared in the case of excessive water injection concentration
(0–0.15–0.2 Pa), in which the quality of SWCNTs decreased.
This phenomenon in the VSSS growth mode brings the possibility to
discuss the etching site by water vapor, that is, a-C on carbon growth
seeds or the edges of SWCNTs. If we assume the edge of newly grown
SWCNTs is preferentially etched by water, the growth rate would be
sensitive to etchant concentration and more likely to decrease once
the partial pressure of water vapor is increased to more than 0.15
Pa. However, the experiment provided an opposite result, an increased
yield of SWCNTs. Thus, we speculate that water vapor tends to etch
a-C randomly on the growth seed surface. Further study is needed to
elucidate the atomistic mechanism of water in the VSSS mode in the
future.The interpretation of the growth results with the water
vapor addition
provides a practical direction for the efficient growth of SWCNTs
from solid growth seeds. Through the reaction between water vapor
and a-C, excessive deposition of carbon source on the growth seed
surface is controlled, which therefore enhanced the lifetime of growth
seeds. The addition of water vapor just after the formation of cap
structures and the precise adjustment of the concentration of etchant
are keys to obtain high-quality SWCNTs with a high yield.
Yield and Quality of SWCNTs Synthesized under
Different Growth Conditions
Figure a compares the yield and the quality of SWCNTs
grown under various conditions from solid carbon particles as growth
seeds. Compared with previous research on one-step growth at 1000
°C,[39] cap engineering using the two-step
growth process developed in this study significantly improves the
growth yield, although the deposition of a-C, which reduces IG/ID, remains. To
solve this impurity problem, water vapor was employed as an etchant
to keep the surface of growth seeds clean. We successfully obtained
highly crystalline SWCNTs with a higher growth yield, which have IG/ID of ∼52
and a G band observation frequency of 40%. The value of the G band
observation frequency demonstrates a significant improvement from
the previous work of 4%.[39] This result
demonstrates the effectiveness of the two-step growth process combined
with water vapor addition.
Figure 5
(a) Variations of the growth yield (G band observation
frequency)
and quality (IG/ID ratio) of SWCNTs according to the control of the initial
growth conditions and the addition of water vapor in the high-temperature
synthesis procedure. Standard deviation was also calculated and presented
as the error bar of averaged IG/ID. (b) SEM image of SWCNTs grown from two-step
growth with water vapor injection, where the initial growth step is
conducted at 850 °C and 1 Pa for 1 min followed by the secondary
growth step at 1000 °C and 0.5 Pa for 30 min. Water vapor was
injected with 0.15 Pa from the beginning in the temperature rising
step.
(a) Variations of the growth yield (G band observation
frequency)
and quality (IG/ID ratio) of SWCNTs according to the control of the initial
growth conditions and the addition of water vapor in the high-temperature
synthesis procedure. Standard deviation was also calculated and presented
as the error bar of averaged IG/ID. (b) SEM image of SWCNTs grown from two-step
growth with water vapor injection, where the initial growth step is
conducted at 850 °C and 1 Pa for 1 min followed by the secondary
growth step at 1000 °C and 0.5 Pa for 30 min. Water vapor was
injected with 0.15 Pa from the beginning in the temperature rising
step.Figure b shows
the SEM image of SWCNTs grown by the two-step growth process with
water vapor injection. Supported by carbon nanoparticle seeds (light
gray particles in Figure b), SWCNTs with a length of a few micrometers are observed.
The SWCNT density of the samples well corresponds to the values of
the G band observation frequency. It should be noted that the length
of SWCNTs is limited by the relatively low efficiency of SWCNT growth
at a high temperature. Based on the present achievement to enhance
the cap formation, future studies on prolonging the growth lifetime
of SWCNTs from solid carbon nanoparticles should further improve the
length and the yield of high-crystallinity SWCNTs.
Conclusions
In conclusion, we developed a cap formation-engineered
two-step
growth process of SWCNTs from solid carbon nanoparticles at a high
temperature by considering the growth driving forces in different
growth stages. We successfully grew highly crystalline SWCNTs with
improved yields. In this growth system, we mainly concentrated on
the initial growth efficiency, which significantly influences the
quality and quantity of the resulting SWCNTs. To fit the higher growth
driving force needed for cap structure formation, a higher partial
pressure of carbon source was selected for the initial growth step.
The effects of growth temperature and time for the initial growth
step were also systematically examined to prevent the deposition of
a-C and to control the formation of SWCNT caps. After achieving a
higher nucleation density of the cap structures, stationary elongation
of SWCNTs was conducted by a secondary growth step. Furthermore, the
deposition of a-C at high temperatures was eliminated by supplying
an etchant, water vapor, to the growth system. By investigating the
injection time and the concentration of water vapor, we optimized
the condition for efficiently removing a-C while preserving the nucleation
of the cap structures. We significantly improved the growth yield,
as evidenced by the increase of the G band observation frequency from
4 to 40% while maintaining a high IG/ID ratio of 52. Our results provide a rational
guideline to synthesize high-quality SWCNTs using high-temperature-stable
solid carbon nanoparticles as growth seeds and will enable various
high-end applications based on SWCNTs that are free from metal impurities,
defects, and a-C.