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Anales AFA Vol. 33 Nro. 4 (Enero 2023 - Marzo 2023) 103-111
https://doi.org/10.31527/analesafa.2022.33.4.103
Materia Condensada
FORMACIÓN DE NANOPARTÍCULAS DE PALADIO POR EL MÉTODO DE LOS
POLIOLES: INFLUENCIA DE LAS CONDICIONES ALCALINAS
FORMATION OF PALLADIUM NANOPARTICLES BY THE POLYOL METHOD:
INFLUENCE OF ALKALINE CONDITIONS
J. F. Sánchez M. 1, H. A. Ritacco 1, M. D. Sánchez *1
1 Instituto de Física del Sur (IFISUR), Departamento de Física, Universidad Nacional del Sur
(UNS), CONICET. Av. L. N. Alem 1253, B8000CPB - Bahía Blanca, Argentina.
Autor para correspondencia: * msanchez@uns.edu.ar
Recibido: 13/06/2022; Aceptado: 01/07/2022
ISSN 1850-1168 (online)
Resumen
Se estudió el efecto del hidróxido de sodio (NaOH) sobre el tamaño de nanopartículas de paladio (Pd)
obtenidas por la ruta del poliol simple. Las nanopartículas se sintetizaron a temperatura ambiente
utilizando cloruro de paladio (II) (PdCl2) y NaOH disuelto en etilenglicol (EG) como promotores de
la reacción de reducción. No se utilizaron agentes protectores ni estabilizadores. Monitoreamos la
cinética de reacción y el crecimiento de las nanopartículas por espectroscopía UV-vis y su
cristalinidad por difracción de rayos X (XRD) en función de la concentración de NaOH. El tamaño
de los cristalitos se evaluó a partir del patrón de difracción. Encontramos que el crecimiento de
nanopartículas está fuertemente influenciado por la relación molar NaOH:Pd. Se obtuvieron tamaños
de cristalitos de 2 a 24 nm para proporciones molares de 1 a 33. A concentraciones más bajas de
NaOH, se encontró que el proceso de nucleación y crecimiento de las nanopartículas estaba controlado
por la reducción de los precursores de iones Pd. A concentraciones más altas, la reducción intermedia
de las especies de Pd-Cl-OH determina la tasa de crecimiento de las nanopartículas que da como
resultado la formación de nanopartículas de tamaño final más pequeño.
Palabras clave: nanopartículas de paladio, hidróxido de sodio, método de polioles, coloides de
paladio.
Abstract
The effect of sodium hydroxide (NaOH) on the size of palladium (Pd) nanoparticles obtained by the
simple polyol route was studied. Nanoparticles were synthesized at room temperature using
palladium(II) chloride (PdCl2) and NaOH dissolved in ethylene glycol (EG) as reduction reaction
promoters. No protective agents or stabilizers were used. We monitored the reaction kinetics and the
growth of the nanoparticles by UV-vis spectroscopy and their crystallinity by powder X-ray
diffraction (XRD) as a function of NaOH concentration. Crystallite size was evaluated from the
diffraction pattern. We found that nanoparticle growth is strongly influenced by the NaOH : Pd molar
ratio. Crystallite sizes from 2 to 24 nm were obtained for molar ratios ranging from 1 to 33. At lower
concentrations of NaOH, the nucleation and growth process of the nanoparticles were found to be
controlled by the reduction of the Pd ion precursors. At higher concentrations, the intermediate
reduction of Pd-Cl-OH species determines the nanoparticle growth rate resulting in the formation of
the smallest final size nanoparticles.
Keywords: Palladium nanoparticles, Sodium hydroxide, Polyol method, Palladium colloids.
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1. INTRODUCTION
The production of nanoparticles from different materials has been a topic of wide interest for
several years. The improvement of techniques, precursors and particle size control have been the main
objectives of previous works [1]. Among the different synthesis techniques, the most popular has been
the polyol method. Presented as a simple, versatile and easy to implement method [2], it has been
successfully applied to a variety of metals [3]. In particular, palladium (Pd) nanoparticles have
received much attention, given their multiple applications, especially in catalysis [4, 5] and
biomedicine [6]. Ethylene glycol (EG) has been commonly used as a solvent and reducing agent in
the production of Pd nanoparticles in a polyol medium [7]. The decomposition of EG produces a
reduction, and the new metallic phase initiates the nucleation and growth that will produce
nanoparticles [8]. However, the reducing power of EG is limited, hence increasing the system
temperature is used to bolster oxidation [9]. The addition of promoting compounds such as hydrazine
[10] or sodium borohydride (NaBH4) [11] is a common practice to facilitate the decomposition of EG
and shorten reaction times. In this way, it is possible to increase the synthesis reaction rate, but it
becomes more difficult to control stabilization and material dispersion in these conditions [12, 13].
Size could potentially be tuned by careful control of temperature, but high temperatures have been
associated with irregular particle growth [14]. Because of these difficulties, the addition of promoters
and surfactants for aggregation control during synthesis has also become a common practice [15].
Although the results of such products are promising, it has been found that chemical residues of
surfactants were chemically adsorbed on the surface of the nanoparticles, potentially compromising
the effectiveness of the produced material for catalytic applications [16]. Wang et al.[17] showed that
it is possible to obtain stabilized noble metal nanoparticles with good dispersion using a protector-
free polyol method. Arora et al. [18] demonstrated that even polyol can act as a stabilizer and that by
controlling solely the reaction conditions it is possible to synthesize monodispersed Pd nanoparticles.
Quinson et al. [19] obtained nanoparticles in surfactantfree EG and studied size control with sodium
hydroxide (NaOH) as a promoter. These studies used the combined effects of promoters and
temperature control to obtain small particle sizes. However, Chen et al. [20] explored the possibility
of using only NaOH to promote nanoparticle synthesis. Since alkaline conditions promote the
reduction of noble metals, it is accepted that the role of NaOH is that of a pH regulator [12].
Nevertheless, it has been observed that hydroxide ions might have an additional catalytic function
[21], affecting the reaction kinetics and therefore the particle size [12, 22]. The amount of hydroxide
(OH) employed is then expected to become a key element in size controlled colloidal synthesis [19,
23]. The aim of the present study was to analyze the influence of hydroxide concentration on the
formation kinetics of Pd nanoparticles by the simple polyol method. No stabilizers were used, and
temperature was kept at room temperature to discard possible effects on the synthesis and particle
size, apart from the OH concentration. We followed the evolution of the metallic precursor reduction
and nanoparticle growth with UV-vis absorbance spectroscopy. Powder X-ray diffraction (XRD) was
used to study the crystallinity, morphology and particle size evolution as a function of NaOH
concentration. In this context, we found that at lower OH concentration both nucleation and grow
process are regulated by the reduction of the Pd precursor given that the induction times are shorter.
As a consequence, few nuclei are created resulting in the formation of larger final size nanoparticles.
The increase in the OH concentration leads to an increase in the induction time as a result of the
formation of Pd-Cl-OH intermediate species. The dissolution of this species regulates the formation
of PdO by increasing the number of nuclei and giving the smallest final size nanoparticle,
independently of the subsequent growth processes that could take place.
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2. METHODS
Materials
Palladium(II) chloride (PdCl2, 99.99%) metal precursor from Spex Industries, Inc. USA, Sodium
hydroxide (Na(OH), 99%) from Merck, KGaA, Germany and Ethylene Glycol anhydrous (EG,
99.8%) from Sigma-Aldrich, Co. USA were used in the synthesis. Acetaldehyde (99.5%), from
Honeywell Riedel-de HaënTM, USA, was also used as a standard of comparison. All reagents used
were analytical grade, stored at room temperature and used without additional purification procedures.
Synthesis of Pd nanoparticles
We obtained Pd nanoparticles by the well-known polyol method [20]. A stock solution of PdCl2
(10 mM) in EG was prepared with the addition of concentrated hydrochloric acid ( 1 µ l HCl : 1 ml
EG) to enhance the PdCl2. By taking different volumes of stock solution and adding NaOH solution
in EG up to a total volume of 5 ml, samples with [NaOH]/[Pd] molar ratios (R) from 1 to 33 were
obtained. The NaOH solution was prepared by diluting a known amount of the base in EG at room
temperature. Before use, all glassware was carefully and thoroughly cleaned and dried.
Mixing was carried out at room temperature and under vigorous stirring. Several minutes after
mixing the reagents, a black colloid deposit containing the nanoparticle materials was observed. To
extract the nanoparticles, the colloid was washed five times with acetone (1:5 vol) in a sonication
(330 W, 50 Hz)-centrifugation (10000 rpm, 10 min) sequence. At each wash, the supernatant was
removed and replaced with fresh acetone. The final material was redispersed in alcohol.
Characterization
Ultraviolet visible absorption spectroscopy (UV-vis).
Synthesis product formation and reaction evolution were followed by UV-vis spectroscopy.
Reactions were carried out in 1 cm quartz cells (1 cm optical pathway) in an Ocean Optics USB2000
spectrophotometer. To ensure a complete and uniform mixture of the reagents, a magnetic stirrer was
used during the spectrum collections. The measurement started when the NaOH solution was added,
at a spectrum measuring interval of 0.1 sec from the 180 to 800 nm wavelength. Further measurements
of the final solution were performed to determine the amount of remaining Pd. In these measurements,
2.5 ml samples were centrifuged (15000 rpm, 10 min) to remove solids, and the supernatant was
analyzed as described above. An acetaldehyde/EG mixture was also analyzed as a reference standard.
Transmission electron microscopy (TEM).
Samples were prepared using droplets of the colloid. These droplets were washed with acetone
and redispersed in methanol. A drop of this suspension was deposited on a carbon-coated copper
microscopy grid (400 mesh). Grids were dried, and the excess liquid was removed with tissue paper.
The grids thus prepared were analyzed using a JEOL-100CX II TEM at 100 kv and a FEI-HR TEM
(TalosTM F200X) at 200 kV.
X-ray diffraction (XRD).
The crystalline structure of the samples was analyzed by powder XRD using a Panaytical
Empyrean III diffractometer with a CuKα (1.5418 Å) radiation. Diffractograms were obtained in the
interval 30 2θ 90, with a step size of 0.02 and a speed of 1 sec/step. Samples were prepared by
drying a few milligrams of the solid material obtained from the colloid after washing.
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3. RESULTS AND DISCUSSION
Formation of Pd nanoparticles
The polyol method employed started with the dissolution of the Pd salt and progressed through
the commonly accepted reactions depicted in Fig. 1. In the particular case of PdCl2, acidification of
the medium is required for complete dissolution. The late addition of NaOH solution would enhance
EG oxidation into acetaldehyde, reducing Pd and producing 2,3-butanedione as main oxidation
product.
The reaction progress can be observed by the naked eye. The initial PdCl2/EG solution (bright
orange) changes color according to the concentration of the added NaOH. A black dispersion, typical
of reduced Pd colloids, can be observed as the NaOH solution is added. This first Pd reduction is fast
FIG. 1: Reduction reaction of metallic ions by ethylene glycol oxidation.
and precedes the nucleation and growth process of nanoparticles. The Pd/EG solutions analyzed by
UV-vis showed two well-defined peaks at 330 and 437 nm. The intensity of these peaks is directly
correlated with the Pd2+ concentration [24], so their attenuation indicates the reduction of Pd2+ and,
therefore, the formation of metallic palladium (Pd0). Thus, we monitored the reaction progress by
following the peak with the highest intensity. In this wavelength interval, no interferences from EG
or NaOH/EG solution are expected.
In preliminary experiments, we observed that the Pd reduction and nanoparticle production were
possible in the absence of NaOH. However, the reaction rate at room temperature was very slow. The
UV-vis spectra from these Pd/EG solutions show different features in comparison to a freshly
prepared solution; however, after several weeks no significant amount of sedimented Pd0 was
obtained.
The spectra (between 190 - 540 nm) of the supernatant solutions at different NaOH concentrations
are shown in Fig. 2. From the PdCl2/EG 10 mM reference solution, the minimum Pd concentration
would be reached at R 4. A precipitate of clustering particles that sediment and leave a translucent
supernatant can be obtained at these concentrations, which implies that all available Pd is reduced and
the Pd2+ peak should not be present. Instead of this peak, two well-defined signals are detected at 220
and 282 nm in agreement with those obtained from the NaOH/EG solution at equivalent
concentrations. As the NaOH concentration increases, the intensity of the peaks increases; the signals
may correspond to by-products formed during the synthesis, probably an acetaldehyde. Analysis of
the EG/acetaldehyde mixture prepared with pure reagents showed peaks at the same wavelengths,
which suggests the presence of remaining acetaldehyde not consumed during the reaction. In this
scenario, the action of NaOH would be mainly catalytic (providing OH ions), increasing the
production of acetyls by EG dehydration [25, 26], according to the first part of the reaction scheme
presented in Fig. 1. The resulting high concentration of acetyls increases the possibility of reduction
of Pd ions and the consequent increase in conversion. There is little evidence in the literature
confirming the presence of acetaldehyde, as it is an unstable compound [27] that might oxidize into
other species easily. In spite of this, Chen et al. [20] identified -CHO groups by infrared spectrometry
in a Tollens reaction and Joseyphus et al. [28] detected acetaldehyde using UV vis with a 2,4-
dinitrophenyl hydrazine test solution. The formation of dioxane, glycolaldehyde and carboxylic acid
has also been suggested, specially at high temperature [23, 29]. A complete discussion on the presence
and quantification of the reaction by-products is beyond the scope of the present study, and further
research is needed.
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Crystalline structure, particle size and morphology
The crystalline structure, average particle size and morphology of the obtained material were
analyzed by XRD and TEM. Fig. 3 shows the diffraction patterns for different NaOH concentrations.
Planes (111), (200), (220), (311) and (222) at Bragg angles 2θ of 40.2, 46.6, 68.0, 82.0 and 86.5,
respectively, are identified by comparison with the Crystallography Open Database, COD file
1534921, indicating that the samples are composed of Pd0 in a face-centered cubic (fcc) structure.
These results are in good agreement with those reported by Long et al. [30] for Pd nanoparticles in
EG. In some samples, we observed the presence of sodium oxalate (Na2C2O4), which could be
removed after the purification process. Although the formation of Pd(OH)2 has been suggested [20],
this compound was not detected in our samples.
TEM images showed that the material is formed by irregularly shaped aggregates, as seen in Fig.
4 for the case of R = 10, which is representative of the overall samples. Nevertheless, it can be assumed
that these clusters are formed by smaller particles, although it is difficult to make a proper estimation
of the particle size mainly due to the overlapping caused by the aggregation itself. These aggregates
FIG. 2: UV-vis absorbance (left scale) and remaining Pd concentration (right scale) of Pd-EG solutions for
different R (0-10, as indicated): after completion of the reaction (black solid lines); without NaOH and stored
for four weeks (red dashed double dotted line); fresh acetaldehyde-EG solution (blue dashed dotted line); and
fresh NaOH-EG solution for a similar concentration of R = 4 (green short dashed line). Conditions: [Pd]0 =
10 mM, VTotal = 5 ml, room temperature.
FIG. 3: XRD patterns of Pd nanoparticles for different R, as indicated.
were already described in the literature and attributed to the self-assembling nature of oxalate dianion
[31]. In this context, XRD data were also used to calculate the crystalline domain size to assess the
effect of NaOH concentration on the size of the nanoparticles. The average crystallite size can be
estimated from the width of the powder diffraction peaks. As can be seen, the initially narrow XRD
peaks increase in width as the NaOH concentration increases (Fig. 3). This correlation may suggest a
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direct relationship between nanoparticle size and NaOH/Pd ratio, even when it is difficult to rule out
that the nanoparticles may consist of more than one crystallite.
Fig. 5 shows the average crystallite size as a function of R, obtained from the Williamson-Hall
plot [32, 33]. The average size decreases rapidly from 24 to 4 nm for R < 6, remaining an
approximately constant size of about 2.5 nm for higher NaOH concentrations. This behavior is in
good agreement with those published elsewhere [20, 34].
To obtain more insight about nanoparticle morphology, we evaluated the crystallite sizes for each
diffraction peak by applying the Scherrer equation [32]. The results for different R values are plotted
in Fig. 6. As expected, the average size for each plane increases as the proportion of the Pd precursor
decreases. Furthermore, a noticeable relative growth of the average crystallite size is observed for
planes (111) and (222), while a decrease is expected according to the Bragg angle increase. This result
suggests that the crystallite has a preferential growth in the direction of plane {111} [31, 35, 36].
However, for R less than 3, the differences between the sizes obtained for the plane (111) and the
ones obtained for the plane (222) become larger as R decreases; for values greater than 3, the
difference
FIG. 4: TEM image of Pd nanoparticle aggregates obtained for R = 10.
FIG. 5: Average size of Pd nanoparticles from XRD analysis.
becomes negligible. Therefore, it can be assumed that the nanoparticles have a nonspherical shape
and that their anisotropy increases as R increases.
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FIG. 6: Average crystallite size of Pd nanoparticles for different R obtained from XRD analysis by applying
the Scherer equation.
Nanoparticle formation process
The kinetic study of nanoparticle formation was performed by in situ UV-vis data analysis of the
reaction, without stabilizers. The omission of stabilizing agents allowed the analysis of the process
without diffusional or mass transfer limitations that might have originated by the use of these
substances. In this way, the maximum formation speed of the nanoparticles can be determined [37].
Fig. 7 shows the absorbance at 437 nm as a function of time for different R values. This process occurs
differently in each case, and the plotted curves vary according to the time interval and the NaOH
concentration used. The identified stages are in agreement with typical nanoparticle formation
mechanisms [38, 39]. The reduction reaction starts at the time tad when NaOH is added to the
PdCl2/EG reference solution. Thereafter, the absorbance sharply drops due to a combination of
dilution and Pd reduction effects. At this stage, seed nuclei appear and would eventually develop into
nanoparticles. Following this stage, the absorbance increases owing to the dispersion produced by the
nuclei growth. This growth continues until the ripening phase is reached, at which point Pd2+ ion
concentration is minimum and larger particles would continue to grow at the expense of smaller ones.
This particle coarsening has been studied in the formation of metallic nanoparticles [40, 41]. As the
reagent concentration increased, the time difference between nucleation and growth was greater and
maturation was clearly observable. Under these conditions, the results are similar to those reported by
Tojo et al. [42] in obtaining metallic particles in a confined environment. When the amount of reagent
is increased, the formation of nuclei is favored and the amount of Pd+ decreases. However, if the
reducing agent is not strong enough, unstable nuclei will form, redissolve and condense on the surface
of more stable ones. For this reason, the total number of particles decreases causing a dispersion
reduction, which eventually leads to an absorbance drop. Finally, the absorbance signal becomes
noisy due to the effect of continuous aggregation and precipitation of larger particles. In all
experiments, a rapid reduction step was observed, with the minimum absorbance being recorded a
few seconds after the start of the reaction. However, the reaction was not completed in all cases. At
low NaOH concentrations, this variation is approximately 45%, and increases to 93% at the maximum
concentration. It has been reported that reduction processes would have a direct effect on the
formation of nuclei, and therefore also on the final nanoparticle sizes [43].
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FIG. 7: Evolution of the absorption for reactions with different concentration of NaOH as a function of time
at room temperature, [Pd]0 = 10mM, Vtotal = 5 ml.
To study these processes, the first step was addressed using the slope of the curve (absorbance
versus time) at the beginning of the reaction. Experimental data for the different reactions are
presented in Fig. 8. Initial rate (starting slope) values along with the R concentrations values are
presented in Fig. 9a. and the final average nanoparticle size along with initial rates in Fig. 9b. These
results suggest the existence of two underlying mechanisms that would affect nanoparticle size in
relation to the NaOH concentration. At lower concentration (R = 0 to 2) the reduction rates increase
from 0.5 s1 up to 2.4 s1 and the average particle size drops from about 18 nm up to 10 nm. For
higher values of R, the reduction rate decreases to a minimum of 0.7 s1, which was not altered with
further increases of R. In agreement with this behaviour, the particle size decreases to a minimum of
around 3 nm for the highest R values tested (Fig. 9b).
Once the absorbance minimum was reached, an induction period became apparent, which precedes
an increase in the UV-vis signal (see Fig. 7). We defined this induction period (ti) as the time in which
absorbance does not vary, that is, from dA/dt 0 until the rate of increase is continuous and greater
than 0.2 s1 (which is the minimum absorbance change that can be detected by our equipment).
FIG. 8: Absorbance (λ = 437 nm) vs. time of the initial region of the Pd2+ reduction curves at different R.
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FIG. 9: (a) Initial rate for different R ratios. (b) Particle size function of the initial rate, (R value is indicated).
Fig. 10 shows how ti increases with R and a linear correlation from R = 2. The maximum value of
ti was 20 min, achievable at R = 33, after which a barely perceptible ( 0.2 s1) increase in absorbance
occurs, probably due to the noise produced by the aggregation of the nanoparticles. These results
indicate that as the NaOH concentration increases, ti also increases, which is indicative of the
formation of small-sized nanoparticle.
At the end of the induction period, the absorbance increase rate is different for each case. For R
< 3, ti is very short and the experimental data can be represented by the first-order kinetic law, dA/dt
= k A, where k is the kinetic constant. A plot of ln A against time would correspond to a straight line
(see Fig. 11a), being the slope the rate constant. A similar experimental behavior was observed by Cai
[44] in silver nanoparticle formation kinetics and by Sau [45] in a seed particle-mediated synthesis.
When R is increased (3, 4), the reduction increases, a longer induction time is recorded and finally a
rapid increase in absorbance is observed. At this point, the nucleation and growth stages begin to be
distinguished separately. For higher R (6, 8), the induction time continues to increase and the growth
kinetics can be fitted using a sigmoidal curve, suggesting an autocatalytic reaction. If this autocatalytic
stage exists, then ln [a / (1-a)] will change linearly with time, where a = Af /At and At and Af are the
absorbance at t and final times, respectively [46, 47]. This is plotted in Fig. 11b; the growth is actually
autocatalytic, which becomes less pronounced with the increase of R. At high R values, the growth
rate and the slope of the curve are so low that the absorbance versus time could be described by a
straight line (linear growth, Fig. 7).
FIG. 10: (a) Induction time for different R ratios. (b) Particle size function of the induction time, (R is
indicated).
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FIG. 11: (a) Absorbance as a function of reaction time (first-order growth). (b) Plots of ln(a/(1-a) as a function
of reaction time (autocatalytic growth).
Influence of NaOH concentration
The different behaviors seen in Fig. 7 could be explained on the basis of the initial NaOH
concentration. This concentration would determine the reduction reaction rate and the following
nucleation and growth steps. Initially, when R < 2, the reaction rate is low. The concentration of Pd
ions remains high given the weak reduction character of the solution, thus few nuclei will form. Then,
the first particles formed act as catalysts, attracting precursor ions to their surface, where they would
be subsequently reduced [48-50]. The low OH concentration delays the reduction process, and
therefore could increase the adsorption of precursor ions to the newly formed nuclei. Furthermore,
the absence of capping agents or other protective agents allows easy access of ions to the surface of
the catalytic nuclei. In addition, since there is a high material flow to the surface, both reduction and
growth occur simultaneously, speeding up the increase in the average size of the newly formed
particles. Reported studies have proved that high concentrations of a strong reducing agent promote
fast initial reduction and the formation of a large number of small nuclei. In other words, the average
particle size decreases as the concentration of the reducing agent increases. In the present study. we
found that the initial rate decreases as the amount of hydroxide increases (Fig. 10a). This relationship
could be indicative of a deceleration of the reduction process; consequently, the nanoparticles formed
will tend to grow. However, no larger nanoparticles were observed. To study this phenomenon, we
followed the evolution of the UV-vis spectra of each reaction as we increased the NaOH concentration
from R = 0 to 33. Fig. 12a shows the absorbance spectra corresponding to zero induction time, ti, for
each reaction. As the reaction progresses from the NaOH addition (tad) to the beginning of the
induction period, ti, for R > 2 the intensity of the 437 nm peak decreases, and also shifts to lower
wavelengths as shown in 12b for the extreme case of R = 33. Initially, this occurs by nonisosbestic
behavior, implying that the starting Pd (Pd2+) is transformed into an intermediate ionic complex [51]
(possibly of the Pd-Cl- OH type), which will eventually decompose and reduce to Pd0. The speciation
of Pd has been researched [52, 53], and published results show that the species distribution is highly
pH dependent. Under acidic conditions, only [PdCl4]2 type ions are present [54]; as pH increases,
these species gradually disappear and start forming complexes of [PdClm(OH)n]2-type composition
that end up being the predominant species [55]. Mechanisms for the formation of these complexes, in
which NaOH is used as the reducing agent, have been proposed in the polyol reduction process [56].
In the present study, the dissolution of Pd chloride was performed in acidic medium (pH = 2), so the
predominant complexes would be tetrachloropalladates. Thus, the observed variations in the UV-vis
are due to the decrease in the concentration of these compounds. For higher R values, along with the
reduction, the formation of chloro-hydroxo complexes occurs, showing that absorption bands are
lower wavelengths. The UV-vis signal variation then corresponds to both the reduction of Pd
[PdCl4]2 and the formation of a new complex, decreasing the intensity and shifting the signal,
11
respectively. This behavior is pronounced as the concentration of OH ions increases, so the initial
reaction rate is lower [57]. The formation of intermediates also limits growth, decreasing the average
particle size. The strong reducing character of the solution (R > 3) creates many small nuclei, which
do not have the ability of attracting precursor ions to trigger autocatalytic surface growth, as these
would not be available. The intermediates compete for these ions and become a regulated supply store
of Pd2+ [58].
FIG. 12: (a) Variation of the characteristic Pd absorption bands for different R when the induction time is
equal to zero. (b) Maximum absorbance peak evolution for R = 33.
The slow dissolution of the intermediates would control the eventual Pd reduction [28], governing
the formation of new nuclei and the increase in size of the nanoparticles [56]. This behavior will
produce a lower growth rate, as indicated by longer induction times, and a steeper slope in the growth
curve as R increases.
These observations indicate that NaOH not only regulates the pH in the EG nanoparticle synthesis
reaction. It Initially acts by promoting the EG oxidation, which will increase the rate of the reaction,
therefore reducing the average size of the formed nuclei. At the same time, the remaining hydroxides
could interact with metal ions, capturing them from the solution and preventing them from
participating in the autocatalytic growth step. The process involves a simultaneous reduction of Pd
ions and the formation of intermediate species, which are determining factors in the control of the
reduction reaction and the size of the nanoparticles.
4. CONCLUSIONS
Palladium nanoparticles were obtained by NaOH-promoted EG reduction at room temperature.
The nanoparticle formation process was analyzed by UV-vis spectroscopy, and the influence of the
NaOH concentration was studied. A typical three-stage mechanism (reduction, nucleation and
autocatalytic growth) was observed in the formation of the nanoparticles. The reaction involves the
formation of an intermediate Pd species (Pd-Cl-OH), which decomposes into Pd0. The dependence of
the average particle size on the initial OH concentrations is attributed to the formation of this
compound, which competes for the available Pd2+ ions and thus modifies the growth kinetics. Hence,
the hydroxide acts as a catalyst that promotes EG decomposition and simultaneously as a regulator of
the amount of Pd ions available for reduction. The overall effect observed is a control of the average
nanoparticle size, which is in the range of 24 to 4 nm as R increases to a value between 4 and 6, and
then stabilizes around 3 nm for higher values of R. As we show by means of XRD analysis, the
resulting nanoparticles have a preferential growth along the plane {111} direction; therefore, they are
nonspherical in shape with an increasing anisotropy as R decrease. Our results show that for this
synthesis process increasing the concentration of NaOH lengthens the induction times, resulting in
the generation of more nuclei, which determines the smallest final particle size independently of
subsequent growth processes.
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Acknowledgements
This work was supported by the Agencia Nacional de Promoción Científica y Tecnológica (ANPCyT),
Argentina [PICT-2019-3185]; the Consejo Nacional de Investigaciones Científicas y Técnicas
(CONICET), Argentina [PIP GI n 11220200101754CO]; and Universidad Nacional del Sur (UNS),
Argentina [PGIUNS 24/F080 and 24/F082].
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