A new approach is presented to overcome the disadvantages of oxidation and harsh sintering conditions of Cu nanoparticle (Cu NP) conductive inks simultaneously. In this process, oleylamine (OAM) adsorbed on particles was effectively eliminated via the reactive desorption by formic acid in alcohols; meanwhile, Cu ion was generated on the surface. The desorption of OAM resulted in more severe surface oxidation of Cu NPs. The oxide (Cu2O) and Cu2+ distributed on the Cu NP surface could be reduced to Cu(0) by NaBH4 solution and take on the role of soldering flux to weld particles into a blocky structure. With the compact coalescence of particles without oxides, the resistivity of metal patterns could fall below 20 μΩ·cm and exhibit proper adhesion. Thanks to the sintering of Cu NPs at ambient conditions, the conductive patterns could be facilely formed on thermosensitive substrates. As the oxide state of Cu would be reduced during sintering, the partially oxidized Cu nanoparticles could be directly applied to conductive inks.
A new approach is presented to overcome the disadvantages of oxidation and harsh sintering conditions of Cu nanoparticle (Cu NP) conductive inks simultaneously. In this process, oleylamine (OAM) adsorbed on particles was effectively eliminated via the reactive desorption by formic acid in alcohols; meanwhile, Cu ion was generated on the surface. The desorption of OAM resulted in more severe surface oxidation of Cu NPs. The oxide (Cu2O) and Cu2+ distributed on the Cu NP surface could be reduced to Cu(0) by NaBH4 solution and take on the role of soldering flux to weld particles into a blocky structure. With the compact coalescence of particles without oxides, the resistivity of metal patterns could fall below 20 μΩ·cm and exhibit proper adhesion. Thanks to the sintering of Cu NPs at ambient conditions, the conductive patterns could be facilely formed on thermosensitive substrates. As the oxide state of Cu would be reduced during sintering, the partially oxidized Cu nanoparticles could be directly applied to conductive inks.
Printed
electronics are a set of electronic devices manufactured
using large-scale and high-volume printing techniques. Owing to their
capability of bypassing conventional high-priced and inflexible silicon-based
electronics to manufacture a variety of devices on flexible substrates,
printed electronics have attracted increasing attention in the field
of electronic devices.[1] Various studies
have illustrated that printed electronic technology is becoming an
effective exploratory method to fabricate large-area and flexible
electronic devices via patterning functional material-based inks.[2] In these inks, solution-processable conductive
inks play an important role in preparing conductive circuits.Recently, metallic nanomaterial conductive inks have been used
as core materials with the implementation of printing techniques such
as inkjet printing. For example, Ag nanomaterial has been widely applied
in conductive inks due to its high conductivity and oxidation resistance.
However, high cost and electromigration phenomenon hinder its widespread
use. In contrast, Cu nanomaterial is considered as the most promising
substitutive material due to its low price, high conductivity, and
excellent electromigration resistance.[3,4] However, Cu
nanomaterial inks are susceptible to oxidation in every step in applications
such as storage, printing, and sintering,[5] which results in deterioration of their electrical conductivity
and increase of the sintering temperature. To overcome the drawback
of oxidation, core–shell nanomaterials with copper as the core
were commonly prepared and applied.[6−8] Although the core–shell
nanoparticles possess excellent oxidation resistance, the complex
preparation could largely limit their applications.Another
challenge in using nanometallic inks is the need for a
high-temperature postprinting process, which increases the cost and
limits the choice of flexible substrates. Usually, bulky capping agents
are used to protect nanomaterials from aggregation. Thus, a sintering
step is necessary for nanomaterial coalescence and impurity removal.[9] For air-sensitive Cu nanoparticles, the sintering
process should be conventionally conducted in an inert or reducing
environment, which further complicates the process.[10,11] Moreover, high-temperature sintering (>200 °C) restricts
the
use of inks on thermosensitive substrates such as paper, plastic,
and fabric.[12] To avoid heat damages of
substrates, researchers have proposed chemical processes to sinter
Ag or Cu@Ag nanoparticle inks at room temperature (RT) in air.[5,13−16] As for Cu nanoparticle inks, Lee et al. attempted to exclude the
additional sintering process by employing Cu NPs treated with poly(VI-co-VTS) and obtained a room-temperature resistivity of 1.2
× 104 μΩ·cm for Cu patterns.[9] However, the resistivity is far from the conductive
demand because of the lack of sintering. To the best of our knowledge,
there are few reports on the formation of satisfactory conductive
patterns from Cu nanoparticle inks at ambient conditions.In
this work, we present a new procedure to overcome both problems
of oxidation and harsh sintering conditions of Cu nanoparticle conductive
inks simultaneously. Reactive sintering at ambient conditions was
achieved by a simple two-step process. To remove the capping agent
from Cu nanoparticles, the patterns were first dipped in formic acid
solution for a few seconds. Oleylamine (OAM) adsorbed on particles
was removed quickly; meanwhile, Cu ion was generated on the surface.
The effective OAM desorption triggers more severe surface oxidation
of Cu NPs. The oxide (Cu2O) and Cu2+ on Cu NPs
could be reduced to Cu(0) by NaBH4 solution and take on
the role of soldering flux to weld particles into a blocky structure.
With the compact coalescence of particles, the resistivity of the
metal patterns could fall below 20 μΩ·cm and exhibit
proper adhesion.
Results and Discussion
Reactive Sintering of Cu NPs
It is
well known that amine can react with acid to produce ammonium salt
or amide. Mazumder et al. found that the OAM-capped nanoparticles
could be readily “cleaned” by acetic acid washing, resulting
in the desorption of OAM.[17] In this work,
we choose formic acid as a stronger acid to detach OAM more efficiently.
The reaction of amide formation usually requires a long reaction time
and high temperature or the help of a catalyst.[18] While the sintering process was realized at RT in less
than 3 min, the formation of amide was unlikely to be the main reaction.
Thus, it is believed that HCOOH reacted with OAM to obtain the ammonium
salt during sintering, as shown in Scheme .
Scheme 1
Reaction of OAM and HCOOH
Due to the firm adhesion of the metal film on the substrate,
the
sintered metal coating could not be obtained in sufficient quantity
for analysis. To clarify the mechanism of sintering, we conducted
similar treatments on Cu NP powders. To confirm the removal of the
OAM layer by HCOOH solution, the powders were immersed in 10 vol %
HCOOH ethanol solution for 3 min and analyzed by thermogravimetric
analysis (TGA) measurements. The release temperature of pure OAM is
about 150 °C, whereas the OAM adsorbed on particles start to
lose weight at around 200 °C.[10] Thus,
dividing the mass loss above 200 °C by the mass at 200 °C
was regarded as the amount of OAM adsorbed on particles. Table summarizes the amount
of OAM adsorbed on particles after different treatments. It can be
seen that the OAM residues dramatically decreased from 11.4 to 7.0%
after a 3 min immersion in 10 vol % HCOOH ethanol solution. Then,
on dipping in 3 wt % NaBH4 aqueous solution for 3 min,
the OAM residues could be further reduced to 2.4%. When the solvent
in step I was replaced with methanol, the decrease of OAM residues
was more remarkable.
Table 1
OAM Residues on Particles
Based on
TGA Measurements from Figures S1–S3
immersion
condition
solvent
untreated
alcohols
10 vol % HCOOH
10 vol % HCOOH + 3 wt % NaBH4
OAM residues
(%)
ethanol
11.4
9.3
7.0
2.4
methanol
8.8
2.2
1.0
Yi et
al. considered that OAM on nanoparticles could act as a barrier
network to inhibit the accessibility of formic acid on the particle
surface due to the high polarity of HCOOH.[19] The permeation of HCOOH in CH2 chains of OAM is harder
than monohydric alcohols. When the powders were immersed in pure HCOOH,
the OAM residues remained at a high level at 11.1% (Table ). In contrast, the OAM residues
were decreased to 9.3% after immersing in pure ethanol. These results
again suggest that it is difficult for HCOOH to access the particle
surface. Thus, the reasonable explanation is that OAM on particles
is first dissolved by alcohols and is then captured by HCOOH to prevent
OAM from readsorption. HCOOH and alcohols could mutually promote the
removal of OAM adsorbed on particles. It was also found that the OAM
residues on the powders treated by 20 vol % HCOOH ethanol solution
were less than those on the powders treated by 10 and 30 vol %, as
shown in Table . At
lower HCOOH concentrations, OAM removed by ethanol could not be effectively
reacted with HCOOH in time. The reaction rate of HCOOH with OAM is
the rate-limiting step, resulting in a better removal efficiency of
20 vol % than 10 vol % HCOOH solutions. Conversely, a higher concentration
of HCOOH would reduce the amount of ethanol and retard the OAM removal
from the particle surface. Eventually, the increase of HCOOH concentration
did not elevate the final removal efficiency, which is seen as a result
of 30 vol % HCOOH solution treatment.
Table 2
OAM Residues
on Particles after Immersing
in Different Concentrations of HCOOH Ethanol Solution Based on TGA
Measurements from Figure S4
HCOOH concentration
10 vol %
20 vol %
30 vol %
100 vol %
OAM residues (%)
7.0
4.0
5.1
11.1
Through the above treatment, most OAM adsorbed on
particles could
be detached. The OAM removal by HCOOH alcohol solutions was also confirmed
by Fourier transform infrared (FT-IR) spectra of HCOOH immersion liquids,
as shown in Figure . To concentrate the detached OAM, 10 vol % HCOOH ethanol immersion
liquid was dried at 0.001 MPa and 50 °C to remove ethanol and
excess HCOOH. The sample had the features of both OAM and copper formate
(Cuf). The peak around 1729 cm–1 related to C=O
of HCOOH was not detected, proving that HCOOH had been removed in
the drying process. The peaks around 3200–3400 cm–1 belonged to the stretching vibration of N–H, and the peaks
of 1600 and 795 cm–1 were the in-plane and out-of-plane
bending vibrations of N–H. This suggests that OAM adsorbed
on particles could be eliminated by HCOOH alcohol solutions. It should
be noted that the bond observed at 832 cm–1 was
attributed to Cu–O vibration, reflecting the ligand’s
carboxyl group that formed the bond with the Cu(II) center in Cuf.[20,21] The double sharp peaks around 1575 and 1374 cm–1 represent the asymmetric and symmetric stretching vibrations of
carboxylate, indicating the formation of Cuf. When the particles were
immersed in HCOOH solution, a part of the Cu oxides on the particles
would react with HCOOH to generate copper formate.
Figure 1
FT-IR profiles of OAM,
10 vol % HCOOH (EtOH) immersion liquid treated
in vacuum, Cuf, and HCOOH.
FT-IR profiles of OAM,
10 vol % HCOOH (EtOH) immersion liquid treated
in vacuum, Cuf, and HCOOH.With the lack of OAM as the capping agent, the Cu NPs were prone
to further oxidation. The X-ray diffraction (XRD) patterns in Figure show that the intensities
of Cu2O peaks become stronger after 10 vol % HCOOH ethanol
immersion. Furthermore, the oxide of Cu could react with HCOOH to
generate Cuf but is inadequate to be detected by XRD, whereas the
dissolution of copper ions was confirmed by analyzing the immersion
alcohol solution. Cu2+ was detected at 5.8 ppm in 10 vol
% HCOOH ethanol immersion using an atomic adsorption spectrometer
(AAS). To confirm that a part of Cu2+ remained on the pattern,
the film was then immersed in deionized water (pH 7). Cu2+ was detected in the immersion water as 0.3 ppm. This means that
not only Cu2O but also Cu2+ was present on the
surface of Cu NPs, as schematically presented in Figure . Thus, Cu2+ could
distribute among the particles’ surface, resulting in a strong
interconnection of the particles. As seen from the transmission electron
microscopy (TEM) images in Figure , the average diameter of the original particles was
11.9 nm (σ = 14.9%). However, the profile of the particles became
ambiguous after HCOOH ethanol immersion, indicating the interconnection
of particles, which may result from Cu2+ distribution.
Figure 2
XRD patterns
of the particles: as-synthesized, 10 vol % HCOOH (EtOH)
immersion, followed by 3 wt % NaBH4 solution immersion.
Figure 3
TEM images of the particles: (a) as-synthesized, (b) 10
vol % HCOOH
(EtOH) immersion, (c) followed by 3 wt % NaBH4 solution
immersion.
XRD patterns
of the particles: as-synthesized, 10 vol % HCOOH (EtOH)
immersion, followed by 3 wt % NaBH4 solution immersion.TEM images of the particles: (a) as-synthesized, (b) 10
vol % HCOOH
(EtOH) immersion, (c) followed by 3 wt % NaBH4 solution
immersion.Subsequently, NaBH4 solution reduced the oxide (Cu2O) and Cu2+ to Cu(0) and led to the strong fusion
among particles. The peaks of Cu2O disappeared after NaBH4 treatment in Figure . From the XRD spectra, the mean Cu crystal size of the particles
was decreased from 7.3 to 5.9 nm after 10 vol % HCOOH (EtOH) immersion
and increased to 14.2 nm through 3 wt % NaBH4 solution
immersion. The crystal size reduction after 10 vol % HCOOH (EtOH)
immersion was due to further oxidation of Cu, resulting in the decrease
of Cu(0) atoms. Moreover, the oxide state of Cu on the surface could
protect Cu(0) particles from agglomeration. On the contrary, NaBH4 solution immersion could reduce the oxide state of Cu and
coalesce the particles, hence the crystal size increased to 14.2 nm.
Most of the particles coalesced together and developed a blocky structure,
as shown in Figure c. Because the pH of NaBH4 solution is high enough to
avoid the dissolution loss of Cu2+, Cu2+ could
act as soldering flux to weld particles. No Cu2+ could
be detected in the NaBH4 immersion solution by AAS. With
the coalescence of particles, OAM adsorbed on particles would be squeezed
out eventually. As described in Table , on being dipped in 3 wt % NaBH4 solution
for 3 min, the OAM residues could be further reduced. The mechanism
of sintering is illustrated in Figure .
Figure 4
Schematic illustration of the chemical sintering mechanism.
Schematic illustration of the chemical sintering mechanism.
Effect of Alcohols
Figure shows the
resistivity of the
metal layer treated by 10 vol % HCOOH alcohol solution, then by 0.75
wt % NaBH4 immersion for different time periods. On prolonging
the dipping time, the resistivity dramatically decreased first and
finally tended to be stable. It should be noted that the optimum resistivity
was 24.38 μΩ·cm (ethanol as the solvent) and 16.93
μΩ·cm (methanol as the solvent). This means that
the selection of the solvent in step I has a significant influence
on the resistivity of Cu films. Methanol seems to have a positive
effect. This result is consistent with that reported by Wakuda et
al. They showed that the removal of alkyl amine from Ag nanoparticles
by methanol was superior to that by ethanol; therefore, the resistivity
of the Ag film dipped in methanol was better than that in ethanol.[22]
Figure 5
Final resistivity of the metal layer treated by HCOOH
solution
and followed by 0.75 wt % NaBH4 immersion for different
time periods. (a) 10 vol % HCOOH in ethanol and (b) 10 vol % HCOOH
in methanol.
Final resistivity of the metal layer treated by HCOOH
solution
and followed by 0.75 wt % NaBH4 immersion for different
time periods. (a) 10 vol % HCOOH in ethanol and (b) 10 vol % HCOOH
in methanol.To clarify the removal efficiency
of OAM by different alcohols,
Cu NP powders were dipped in methanol or ethanol for 3 min and then
analyzed by TGA measurements. The results in Table showed that OAM residues were reduced from
11.4 to 8.8 and 9.3% by methanol and ethanol, respectively. Due to
the superior removal efficiency, the OAM residues on Cu powders treated
by 10 vol % HCOOH in methanol were far less than those on Cu powders
treated by 10 vol % HCOOH in ethanol solution (2.2 vs 7.0%), as shown
in Table . Benefiting
by the higher removal efficiency in methanol, we obtained lower resistivity
by dipping the film in 10 vol % HCOOH methanol.
Effect of HCOOH Concentration
As
described previously, the Cu oxide could react with HCOOH to generate
copper formate. The dissolution of Cu ion in alcohol solution would
lead to the loss of copper. Thus, it is essential to explore the relationships
between Cu loss and HCOOH concentration. The Cu ion content in the
immersion liquid was used to measure the Cu loss, as shown in Figure . As the concentration
of HCOOH increased, the Cu ion content increased, indicating the augmented
Cu loss. Obviously, this is because the increasing concentration of
the reactant (HCOOH) accelerated the formation rate of Cu ion. Moreover,
the Cu loss in methanol solution was higher than that in ethanol under
the same HCOOH concentration. This result seems related to the higher
removal efficiency of OAM in methanol, which leads to the exposure
of Cu particles.
Figure 6
Cu2+ content in HCOOH alcohol immersion liquid.
Cu2+ content in HCOOH alcohol immersion liquid.To quantify the effect of HCOOH concentration on
resistivity, the
coating films were immersed in HCOOH ethanol solutions (5, 10, and
20 vol %), then dipped in 0.75 wt % NaBH4 for different
time periods. As shown in Figure a, at the concentration of 5 vol %, the resistivity
was uneven and maintained at a high level due to the large OAM residues.
Even when NaBH4 immersion time was prolonged to 15 min,
the resistivity still remained at 84.38 μΩ·cm. At
higher concentrations of 10 and 20 vol %, the resistivity at both
concentrations significantly decreased to about 25 μΩ·cm
in Figure b,c. This
result illustrates that 10 vol % HCOOH in ethanol is enough to obtain
low resistivity.
Figure 7
Final resistivity of the metal layer treated by HCOOH
solution,
followed by 0.75 wt % NaBH4 solution for different time
periods. (a) 5 vol % HCOOH in ethanol, (b) 10 vol % HCOOH in ethanol,
(c) 20 vol % HCOOH in ethanol, (d) 5 vol % HCOOH in methanol, and
(e) 10 vol % HCOOH in methanol.
Final resistivity of the metal layer treated by HCOOH
solution,
followed by 0.75 wt % NaBH4 solution for different time
periods. (a) 5 vol % HCOOH in ethanol, (b) 10 vol % HCOOH in ethanol,
(c) 20 vol % HCOOH in ethanol, (d) 5 vol % HCOOH in methanol, and
(e) 10 vol % HCOOH in methanol.When only the solvent was replaced with methanol, the resistivity
could be reduced to less than 20 μΩ·cm, as shown
in Figure d,e. The
lowest resistivity reached 16.93 μΩ·cm, only 10 times
the resistivity of bulk copper. Moreover, 5 vol % HCOOH in methanol
was high enough to achieve a low resistivity of 19.40 μΩ·cm
in Figure d. The resistivity
of 20.23 μΩ·cm was obtained after 3 min immersion
in 0.75 wt % NaBH4 solution. This is largely due to the
high OAM removal efficiency of HCOOH methanol solution. As described
above, the Cu loss in 5 vol % HCOOH methanol solution was close to
that in 10 vol % HCOOH in ethanol solution, whereas the Cu films possessed
a lower resistivity. Therefore, 5 vol % HCOOH methanol solution for
step I is economic and efficient for reactive sintering.
Effect of NaBH4 Concentration
At the second
step of sintering, the concentration of NaBH4 may influence
the structure of the metal film and the final
resistivity. Higher concentrations could guarantee sufficient reaction
and thorough coalescence. The coatings were immersed in 10 vol % HCOOHethanol solution then dipped into different concentration of NaBH4 for 3 min. With the increase of NaBH4 concentration,
the resistivity decreased to 21.68 μΩ·cm at 3 wt
% (Figure a). As shown
in Figure b,c, most
of the particles coalesced throughout the whole thickness of the coating
and not only in the surface. Due to the small thickness (approximately
350 nm), the sintering agent could reach deep into the interior of
the coating and developed a blocky connected structure. On further
increasing the concentration to 4 wt %, the resistivity dramatically
elevated to 87.71 μΩ·cm due to the severe damage
of the metal film, as shown in Figure e. The broken film resulted from the vigorous reduction
reaction that occurred as the NaBH4 concentration reached
4 wt %. However, when the film was treated by 3 wt % NaBH4, and even extended the immersion time to 40 min, it remained uniform
without any damages, as shown in Figure f.
Figure 8
(a) Resistivity of the metal layer treated by
10 vol % HCOOH ethanol
solution, followed by different NaBH4 concentrations for
3 min. (b, c) Scanning electron microscopy (SEM) images of Cu layer
after immersing in 3 wt % NaBH4 for 3 min and (d–f)
scanned images of metal films sintered with different concentrations
of NaBH4 for 3 min.
(a) Resistivity of the metal layer treated by
10 vol % HCOOH ethanol
solution, followed by different NaBH4 concentrations for
3 min. (b, c) Scanning electron microscopy (SEM) images of Cu layer
after immersing in 3 wt % NaBH4 for 3 min and (d–f)
scanned images of metal films sintered with different concentrations
of NaBH4 for 3 min.As for 10 vol % HCOOH methanol solution, 3 wt % NaBH4 immersion
caused film damage, as shown in Figure b. Only when the concentration of NaBH4 was
below 1 wt %, the metal films could remain even in appearance.
However, the resistivity in Figure a increased from 16.93 to 25.89 μΩ·cm
as the concentration of NaBH4 increased from 0.75 to 1
wt %. This change indicates that internal damages of the film occurred
with 1 wt % NaBH4 immersion. Thus, the films treated by
10 vol % HCOOH methanol solution were more fragile. Because of the
lower OAM residues as described above, the oxidation of Cu was more
severe and resulted in a fast reduction reaction in step II. Meanwhile,
the reduction of OAM residues may also decrease the adhesion of particles.
Figure 9
(a) Resistivity
of the metal layer treated by 10 vol % HCOOH methanol
solution, followed by different NaBH4 concentrations for
9 min. (b) Scanned images of metal films sintered with different concentrations
of NaBH4 for 9 min.
(a) Resistivity
of the metal layer treated by 10 vol % HCOOH methanol
solution, followed by different NaBH4 concentrations for
9 min. (b) Scanned images of metal films sintered with different concentrations
of NaBH4 for 9 min.These results are encouraging because a Cu film with low resistivity
(16.93 μΩ·cm) was obtained by a simple two-step sintering
process at ambient conditions. Moreover, the metal pattern exhibited
proper adhesion. Figure S5 shows the remaining
coating structure after the peel-off adhesion test for sintered samples.
The results show that upon peel-off almost all materials remain at
the substrate.
Conclusions
In summary,
a process for sintering Cu NPs at ambient conditions
was proposed. The sintering was triggered by the removal of the capping
agent and “soldering” through reduction. Oleylamine
(OAM) adsorbed on Cu NPs was effectively eliminated by the reactive
desorption by formic acid in alcohols. Meanwhile, more severe surface
oxidation occurred on Cu NPs and Cu ion was generated. Then, NaBH4 aqueous solution was applied to reduce the oxidation layer
that contained Cu2+ and Cu2O. The oxide (Cu2O) and Cu2+ on the surface of particles could act
as soldering flux to weld particles into a blocky structure. With
the coalescence of particles, OAM adsorbed on particles would be squeezed
out eventually. The resistivity of the metal patterns could fall below
20 μΩ·cm and exhibit proper adhesion.Based
on these findings, sintering can be achieved at ambient conditions,
enabling the formation of conductive patterns on various thermosensitive
substrates. More importantly, the oxidation of Cu nanoparticles would
not hinder the application of Cu NP inks and could even act as soldering
flux to coalescence particles. Furthermore, low-cost, continuous fabrication
processes could be realized using the above simple sintering method.
Experimental Section
Chemicals and Materials
Copper formate
tetrahydrate (98%) was purchased from Alfa Aesar. Oleylamine (OAM,
90%) was bought from Aladdin. Paraffin liquid (CP, distilate temperature
>300 °C) was from Tianjin Guangfu Fine Chemicals Research
Institution.
Hexane (95%), isopropyl alcohol (99.7%), and NaOH (96%) were obtained
from Xilong Scientific Company. Methanol (99.8%) was bought from Tong
Guang Fine Chemicals Company. Formic acid (98%) and ethanol (99.7%)
was purchased from Sinopharm Chemical Reagent Beijing Co., Ltd. NaBH4 (98%) and octane (99%) were supplied by Tianjin Fuchen Chemical
Reagents Factory.Copper formate terahydrate was dried at 0.001
MPa, 90 °C for 12 h to get anhydrous copper formate (Cuf). Other
chemicals were used as received without further purification.
Characterization
The morphology of
particles was investigated by transmission electron microscopy (TEM)
analysis (HT-7700, Hitachi and JEM2010, JEOL), and the size distribution
of particles was obtained by measuring the diameter of more than 100
nanoparticles. The chemical structures of the immersion liquid were
analyzed by a Fourier transform infrared (FT-IR) spectrometer (Tensor
27, Bruker). Additionally, the crystalline structures of particles
were identified by X-ray diffraction (XRD, D8 Advance, Bruker) using
Cu Kα radiation (λ = 1.5406 Å). Thermogravimetric
analysis (TGA, STA 409PC, Netzsch) was used to investigate the thermal
decomposition behavior of organics at 10 K/min. The sheet resistance
of the metal layer was measured using a 4-point probe (RTS-9, 4 Probes
Tech). The surface and cross-sectional morphology of Cu films were
observed using field emission scanning electron microscopy (SEM, SU-8010,
Hitachi). Furthermore, the volume resistivity of the metal pattern
was calculated from the sheet resistance together with the metal layer
thickness determined by SEM. The Cu(II) ion concentrations in the
immersion solution were analyzed by an atomic adsorption spectrometer
(AAS, NITACHI 172-8035).
Cu NP Synthesis and Conductive
Ink Formulation
Cu NPs were synthesized by the decomposition
of copper formate
(Cuf) using oleylamine (OAM) as the complexing ligand and stabilizing
agent as described previously.[10] Cuf (1.2
g) and OAM (9.3 g) were dissolved in 80 mL of paraffin liquid at 50
°C, and the air was removed from the solution by bubbling with
N2. The solution was heated at 170 °C for 30 min under
N2 and cooled with a water bath. Then, the colloid was
centrifuged at 10 000 rpm for 30 min to separate the Cu NPs.
The Cu NPs were washed once with the solvent (hexane/isopropyl alcohol
= 1:1, v/v) before formulating the conductive inks. Finally, 30 wt
% Cu NPs were dispersed in octane using an ultrasonic bath for 2 h
to prepare the conductive ink.
Reactive
Sintering at Ambient Conditions
The sintering process consists
of two steps. The formulated ink
was coated onto a poly(ethylene terephthalate) (PET) film using an
applicator (25 μm, AICE Inc.). In the first step (step I), the
coated PET films were immersed in formic acid solution (5, 10, 20
vol %) for 20 s and rinsed with the solvent (methanol or ethanol).
The above operations were repeated three times to increase the coating
thickness. For the second step (step II), NaBH4 was dissolved
in pH 12 NaOH solution according to different concentrations (1–4
wt %). The films from step I were then immersed into the NaBH4 solution for 0–15 min and washed with deionized water.