# A Novel Synthesis of Gold Nanoparticles Supported on Hybrid Polymer/Metal Oxide as Catalysts for p-Chloronitrobenzene Hydrogenation

Authors: Cristian H. Campos; Bruno F. Urbano; Cecilia C. Torres; Joel A. Alderete
Journal: Journal of Chemistry
 (2017)

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## Abstract

This contribution reports a novel preparation of gold nanoparticles on polymer/metal oxide hybrid materials (Au/P[VBTACl]-M metal: Al, Ti or Zr) and their use as heterogeneous catalysts in liquid phase hydrogenation of p-chloronitrobenzene. The support was prepared by in situ radical polymerization/sol gel process of (4-vinyl-benzyl)trimethylammonium chloride and 3-(trimethoxysilyl)propyl methacrylate in conjunction with metal-alkoxides as metal oxide precursors. The supported catalyst was prepared by an ion exchange process using chloroauric acid (HAuCl4) as gold precursor. The support provided the appropriate environment to induce the spontaneous reduction and deposition of gold nanoparticles. The hybrid material was characterized. TEM and DRUV-vis results indicated that the gold forms spherical metallic nanoparticles and that their mean diameter increases in the sequence, Au/P[VBTACl]-Zr > Au/P[VBTACl]-Al > Au/P[VBTACl]-Ti. The reactivity of the Au catalysts toward the p-CNB hydrogenation reaction is attributed to the different particle size distributions of gold nanoparticles in the hybrid supports. The kinetic pseudo-first-order constant values for the catalysts in the hydrogenation reaction increases in the order, Au/P[VBTACl]-Al > Au/P[VBTACl]-Zr > Au/P[VBTACl]-Ti. The selectivity for all the catalytic systems was greater than 99% toward the chloroaniline target product. Finally the catalyst supported on the hybrid with Al as metal oxide could be reused at least four times without loss in activity or selectivity for the hydrogenation of p-CNB in ethanol as solvent.


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## Body

## 1. Introduction

Aromatic chloramines are an important building block in the synthesis of many fine chemicals, such as dyes, drugs, herbicides, and pesticides [1–4]. Their conversion has been reported employing heterogeneous metal catalysts as polymer-stabilized colloidal metal clusters [5–9], supported metal catalysts on inorganic solids [5–9], supported metal catalysts on inorganic solids [10–14], and polymer-hybrid supports [15–18]. In the preparation of metal supported catalysts, carriers are first treated with metal precursors followed by reduction into metal nanoparticles using H2 in thermic treatment or by coupling them with reducing agents in liquid phase such as hydrazine, formic acid, and urea [19–23]. The metals as Au, Pt, Pd, Ni, and Ir are selective active phases for -NO2 group hydrogenation [10, 21, 24–28], even under mild temperature conditions, especially metallic gold nanoparticles (Au-Nps) [19, 20, 29].Polycationic-metal oxide hybrid systems have recently been used for anions pollutant remediation since they provide a unique opportunity to include permanent cationic charge in organic functional groups [30, 31]. These materials arise as an excellent platform for the preparation of metal supported catalysts because they present the main advantage of being metal anion sorbents. The anionic gold precursor, AuCl4-, can exchange anions with the counterion, leaving the gold in intimate contact with the cationic moiety. In this way, recent reports show the spontaneous ability of some materials to reduce Au3+ cations to gold nanoparticles (Au-Nps), for example, carbonaceous materials [32], polymers materials [33–35], and metal oxide supports [36–39].The aim of this research is the use of hybrid materials made from poly[(4-vinylbenzyl)trimethylammonium chloride] (P[VBTACl]) and three different metal oxides (Al, Ti, and Zr), to produce metal Au-Nps supported catalysts for p-chloronitrobenzene (p-CNB) liquid phase hydrogenation to obtain the respective p-chloroaniline (p-CAN). The novelty of this report is the use of this hybrid material as support to provide a simultaneous reduction/deposition of the gold precursor without any external reducing agent and produce highly selective catalytic system for p-CAN production employing hydrogen as reducing agent.


## 2. Experimental Section

### 2.1. Hybrid Supports Synthesis

The hybrids material synthesis was fully reported in our previous report [40]. The white-yellow solid hybrid polymer/metal oxide prepared was dried in a vacuum oven at 373 K for 1 h and stored in a desiccator under an N2 atmosphere prior to the catalyst synthesis. The material obtained was labeled as P[VBTACl]-M where M: Al, Ti, or Ti corresponds to the metal employed and fully characterized in our previous reports.


### 2.2. Catalysts Synthesis

The catalysts (1.0 g) were prepared at 0.5% Au mass using the P[VBTACl]-M supports. The appropriate amount of support is placed in a round bottom flask with 50 mL of water. A solution containing the required amount of the HAuCl4·H2O was aggregated to obtain the desired metal loading and the system was placed in a temperature regulated bath, for 12 h at 298 K with 300 rpm of magnetic stirring. During this process, the pH was monitored and the composites changed color from yellow to purple. The solids were filtered and washed with deionized water until a low constant conductivity was obtained. The metal loading was monitored by ICP, detecting the residual gold in the first and final filtrate solution after mixing with the composite for all catalysts. Finally, the catalysts were dried in a vacuum oven at 373 K for 1 h and stored in a desiccator under an N2 atmosphere prior to the catalytic tests. These were labeled as Au/P[VBTACl]-M.


### 2.3. Characterization

The metal elemental composition was quantitatively (triplicate) monitored by digesting 50 mg of loaded composite in 10 mL concentrated nitric/hydrochloric (1 : 3) acid solution using microwave-assisted digestion and the samples were analyzed by inductively coupled plasma atomic emission spectrometer (ICP-AES) Perkin Elmer Elas 6000S instrument. N2-BET surface areas and pore volumes were determined on a Micromeritics ASAP 2010 apparatus at 77 K. UV-vis spectra of diffuse reflectance of solid state (DRUV-vis) were studied in the range of 200–900 nm on a Varian Cary 3 UV-vis spectrophotometer equipped with an area of 150 mm in diameter covered with poly integration tetrafluoroethylene (PTFE). The dust samples were mounted in a quartz cell, which provided a sample thickness greater than 3 mm and thus guaranteed “infinite” sample thickness. Electron microscopy were measured using a Transmission Electron Microscope, Philips model CM200 with energy dispersive analyzer and digital camera coupled to a high speed TVIPS FastScan F-114 model of 1024 × 1024 pixels. The samples for analysis were prepared by dispersion in ethanol/H2O (1 : 1) and deposited on a porous carbon/Cu grid (300 Mesh). Up to 300 individual metal particles were counted for each catalyst and the surface area-weighted mean Au diameter (dp) was calculated from(1)dp=∑inidi3∑inidi2,where ni is the number of particles of diameter di. The size limit for the detection of Au-NPs particles on samples was ca. 1 nm. X-ray photoelectron spectra (XPS) were recorded using an Escalab 200 R spectrometer equipped with a hemispherical analyzer and using nonmonochromatic Mg Kα X-ray radiation (hυ=1253.6 eV). The spectra were fitted to a combination of Gaussian-Lorentzian lines of variable proportion. The C 1s core-level of adventitious carbon at a binding energy (BE) of 284.8 eV was taken as an internal standard.


### 2.4. Catalytic Activity

The catalytic assays of p-CNB hydrogenation were performed in a stainless steel, Parr-type batch reactor at a concentration of 0.02 mol L−1 of substrate using absolute ethanol as a solvent and stirring at 800 rpm under 20 bar H2 pressure. All further experiments were carried out in the absence of external mass transfer limitations according with our previous experiments and 0.050 g of catalyst was used for the catalytic measurements. A noninvasive liquid sampling system with in-line filter allowed a controlled removal of aliquots (≤0.5 cm3) from the reactor. All the catalytic experiments were made three times (with fresh catalyst every time) and the average values were reported for kinetic data. The reaction samples were analyzed in a GC-MS Shimadzu GCMS-QP5050. The conversion level and the CAN’s yield were calculated using the following equations:(2)X%=p-CNB0-p-CNBtp-CNB0·100YCAN%=p-CANtp-CNB0·100,where CNB0 is the CNB initial concentration and p-CNBt and p-CANt are the p-CNB concentration and p-CAN concentration at different time, respectively. (3)TOFmin-1=p-CNBhydrogenatedmolSurface metallic Aumol·timemin.The turnover frequency was defined at 20% of conversion. The values for surface metallic were determinate employing the ICP metal content and metallic dispersion.


## 2.1. Hybrid Supports Synthesis

The hybrids material synthesis was fully reported in our previous report [40]. The white-yellow solid hybrid polymer/metal oxide prepared was dried in a vacuum oven at 373 K for 1 h and stored in a desiccator under an N2 atmosphere prior to the catalyst synthesis. The material obtained was labeled as P[VBTACl]-M where M: Al, Ti, or Ti corresponds to the metal employed and fully characterized in our previous reports.


## 2.2. Catalysts Synthesis

The catalysts (1.0 g) were prepared at 0.5% Au mass using the P[VBTACl]-M supports. The appropriate amount of support is placed in a round bottom flask with 50 mL of water. A solution containing the required amount of the HAuCl4·H2O was aggregated to obtain the desired metal loading and the system was placed in a temperature regulated bath, for 12 h at 298 K with 300 rpm of magnetic stirring. During this process, the pH was monitored and the composites changed color from yellow to purple. The solids were filtered and washed with deionized water until a low constant conductivity was obtained. The metal loading was monitored by ICP, detecting the residual gold in the first and final filtrate solution after mixing with the composite for all catalysts. Finally, the catalysts were dried in a vacuum oven at 373 K for 1 h and stored in a desiccator under an N2 atmosphere prior to the catalytic tests. These were labeled as Au/P[VBTACl]-M.


## 2.3. Characterization

The metal elemental composition was quantitatively (triplicate) monitored by digesting 50 mg of loaded composite in 10 mL concentrated nitric/hydrochloric (1 : 3) acid solution using microwave-assisted digestion and the samples were analyzed by inductively coupled plasma atomic emission spectrometer (ICP-AES) Perkin Elmer Elas 6000S instrument. N2-BET surface areas and pore volumes were determined on a Micromeritics ASAP 2010 apparatus at 77 K. UV-vis spectra of diffuse reflectance of solid state (DRUV-vis) were studied in the range of 200–900 nm on a Varian Cary 3 UV-vis spectrophotometer equipped with an area of 150 mm in diameter covered with poly integration tetrafluoroethylene (PTFE). The dust samples were mounted in a quartz cell, which provided a sample thickness greater than 3 mm and thus guaranteed “infinite” sample thickness. Electron microscopy were measured using a Transmission Electron Microscope, Philips model CM200 with energy dispersive analyzer and digital camera coupled to a high speed TVIPS FastScan F-114 model of 1024 × 1024 pixels. The samples for analysis were prepared by dispersion in ethanol/H2O (1 : 1) and deposited on a porous carbon/Cu grid (300 Mesh). Up to 300 individual metal particles were counted for each catalyst and the surface area-weighted mean Au diameter (dp) was calculated from(1)dp=∑inidi3∑inidi2,where ni is the number of particles of diameter di. The size limit for the detection of Au-NPs particles on samples was ca. 1 nm. X-ray photoelectron spectra (XPS) were recorded using an Escalab 200 R spectrometer equipped with a hemispherical analyzer and using nonmonochromatic Mg Kα X-ray radiation (hυ=1253.6 eV). The spectra were fitted to a combination of Gaussian-Lorentzian lines of variable proportion. The C 1s core-level of adventitious carbon at a binding energy (BE) of 284.8 eV was taken as an internal standard.


## 2.4. Catalytic Activity

The catalytic assays of p-CNB hydrogenation were performed in a stainless steel, Parr-type batch reactor at a concentration of 0.02 mol L−1 of substrate using absolute ethanol as a solvent and stirring at 800 rpm under 20 bar H2 pressure. All further experiments were carried out in the absence of external mass transfer limitations according with our previous experiments and 0.050 g of catalyst was used for the catalytic measurements. A noninvasive liquid sampling system with in-line filter allowed a controlled removal of aliquots (≤0.5 cm3) from the reactor. All the catalytic experiments were made three times (with fresh catalyst every time) and the average values were reported for kinetic data. The reaction samples were analyzed in a GC-MS Shimadzu GCMS-QP5050. The conversion level and the CAN’s yield were calculated using the following equations:(2)X%=p-CNB0-p-CNBtp-CNB0·100YCAN%=p-CANtp-CNB0·100,where CNB0 is the CNB initial concentration and p-CNBt and p-CANt are the p-CNB concentration and p-CAN concentration at different time, respectively. (3)TOFmin-1=p-CNBhydrogenatedmolSurface metallic Aumol·timemin.The turnover frequency was defined at 20% of conversion. The values for surface metallic were determinate employing the ICP metal content and metallic dispersion.


## 3. Results and Discussion

### 3.1. Au Nanoparticles Synthesis and Catalyst Characterization

In the catalysts synthesis, the supports were contacted with metal precursor dissolved in aqueous solution to sorb the active phase on the polymer/metal oxide surface. The HAuCl4 can exchange the chloride ligand with hydroxyl anion providing the formation of mixed chlorohydroxy complexes AuCl4-xOHx- as has been reported by Murphy and LaGrange [41]. In other way, P[VBTACl]-M hybrid systems can accumulate gold by ion-exchange process from (1) the poly-cationic quaternary ammonium pending group and (2) metal oxide surface sorption (especially in an acidic range of pH) [41]. The pH measurements could be used to examine the formation of the Au-Nps by spontaneous reduction of metal precursor on the support hybrid materials. Figure 1 shows the plot of pH versus time during the Au-NPs deposition. During the process we observed the change of solution from yellow (typical for HAuCl4 in solution) to purple as a consequence of the gold nanoparticles surface plasmon band [9, 42, 43]. All the composites show a continuous increase in the pH of the solution over time. The initial pH is 3.32 at room temperature for all the composites, though it increases during the course of the preparation to ca. 5.10, 4.58, and 4.80 for P[VBTACl]-Al, P[VBTACl]-Ti, and P[VBTACl]-Zr, respectively.Figure 1
pH versus time for P[VBTACl]/M catalyst synthesis. Conditions: gold (III) chloride hydrate precursor concentration 6.02 × 10−4 mol L−1. Temperature: 298 K and magnetic agitation: 300 rpm. The blank corresponds to the solution of precursor without the support.At the initial pH, the predominant gold species present in the solution are [AuCl3OH]− and [AuCl2(OH)2]−. The reduction of these gold chlorohydroxy complexes proceeds because they possess a minor redox potential compared to [AuCl4]−. The sorption of these species could occur in defect sites of the metal oxide surface. These defect sites could provide electronic transfer from the defects on the surface to the AuCl4-xOHx- species causing gold spontaneous reduction and thus an increase of the pH [33, 37, 38, 44]. This defects are potentials sites for reduction due certainly to the remaining free radicals initiator still trapped into the polymer/metal oxide core as was reported by Féral-Martin et al. [34].Table1 displays the ICP-AES analysis for all the Au catalysts synthesized. The Au metal content is very similar to the nominal one. The specific SBET areas are also summarized in Table 1. These values are similar to the ones of our previous results [40] and they indicate that the supports are not modified upon the impregnation procedure.Table 1
S
B
E
T, Au content, and average Au-NPs size by TEM characterization of Au/P[VBTACl]-M catalysts.
M
S
B
E
T (m2g−1)
ICP-AES(Au%)
d
p (nm)
D
i
s
p
e
r
s
i
o
n
a (%)
Al
11
0.45
5.1
±
2.7
19.5
Ti
9
0.38
10.1
±
3.8
9.9
Zr
10
0.42
4.5
±
2.5
22.2
A
s
s
u
m
i
n
g
a Au homodispersion and the same metal particle size (dp), Au dispersion was calculated using formula D%=1/dTEM×100% [19].Figure2 shows representative TEM images performed to determine the particle size of Au-NPs on the composites reported here. For the Au/P[VBTACl]-Zr and Au/P[VBTACl]-Al catalysts no significant differences in their images are observed. The active phase is randomly dispersed on the composite surface, with metal-particle aggregates particularly visible. Their size distribution is broad but finite ranging from 2.0 up to 10 nm (Figures 2(a) and 2(c)).Figure 2
Representative TEM Micrograph and Au nanoparticle size distribution measurements for Au/P[VBTACl]/M catalysts. (a) M: Al; (b) M: Ti; (c) M: Zr.
(a)
(b)
(c)The Au-NPs supported on P[VBTACl]-Ti feature a more random morphology and particle size distribution, composed of bigger crumb-like crystallites, indicative of low dispersion of Au, and the majority of the particles are in the fraction of 8.0–15 nm. On the other hand, solid structures were detected in this catalyst and were attributed to the segregation of the TiO2 phase as was informed in our previous reports [40].Curiously, P[VBTACl]-Ti was the only one to show a visible inorganic phase segregation after the hybrids synthesis. This behavior could be explained by the fast and spontaneous poly-condensation of the inorganic precursor during the sol-gel synthesis in comparison to Zr and Al metal-alkoxide precursor [45]. The Au-NPs deposited on the support surface showed a preferential deposition around the segregated TiO2-phase as was detected by TEM photographs (Figure 2(b)). On this way, TiO2 could promote a fast reduction of gold ions due to strong binding interactions with oxygen vacancies as was reported by Pan and Xu [38].DRUV-vis spectra of the catalysts are shown in Figure3. For all the Au/P[VBTACl]-M catalysts, an absorption band between 200 and 300 nm was observed. The intensity of the absorption band could be attributed to polymeric phase absorption (π→π∗ transition from benzene pending groups moieties). For Au/P[VBTACl]-Ti catalyst, TiO2 species were detected in the range 330–340 nm, indicating the presence of anatase-phase (with particle size > 5.0 nm) [46] in agreement with TEM and XRD characterization previously reported by Campos et al. [40].Figure 3
DRUV-vis spectra of the Au/P[VBTACl]/M catalyst.The plasmon of Au was observed to be centered between 530 and 560 nm, which indicates that the Au NPs are mostly spherical [47]. The intensity of the plasmon also depends on the particle size [48]. Our results are consistent with a supported metallic Au for all the catalysts where the differences in characteristic wavelength may be the result of differences in Au particle size as was discussed in TEM characterization (see Table 1).In order to get a better knowledge on the active gold state, the Au/P[VBTACl]/M catalysts were characterized by XPS as shown in Table2. Differences in Au 4f7/2 binding energy between the samples were observed. The binding energy (BE) of Au for all catalytic systems showed that Au 4f7/2 appears at 84.0–84.2 eV. This is indicative of the complete reduction of the gold precursor by the hybrid support. This could be attributed to the fact that their BE is close to that reported for metallic Au nanoparticles [21, 29]. The N 1s BE contribution was detected at 404.0–403.9 eV, which is typical for ammonium quaternary groups, while the Cl 2p3/2 at 199.3 eV corresponds to chloride counter ion in agreement with previous reported results by Deng et al. [49].Table 2
Binding energies (eV) of internal electrons and atomic surface ratio of Au/P[VBTACl]-M catalysts.
M
M2p, 3d(eV)
Au 4f7/2 (eV)
N 1s(eV)
Cl 2p3/2 (eV)
Au/Msup
N/Clsup
Al
74.6
84.2
404.0
199.1
0.0102
0.914
Ti
458.6
84.1
403.9
199.0
0.0059
0.814
Zr
182.2
84.0
404.1
199.1
0.0133
1.014The Au/M atom ratio showed a reasonable value for high Au-NPs dispersion for Au/P[VBTACl]-Al and Au/P[VBTACl]-Zr catalysts. Furthermore, Au/P[VBTACl]-Ti system showed a lower Au/Ti atom ratio, which could be attributed to a decrease in the dispersion of Au active phase and consequently an increase in the Au particle size. This shows good agreement with TEM results (see Figure2). Finally, all systems showed N/Cl atom surface ratio close to 1, which indicated that the chloride excess was successfully eliminated from catalyst surfaces (N+cation/Cl-anion).


### 3.2. Catalytic Hydrogenation Reaction

#### 3.2.1. P-CNB Hydrogenation

The results obtained for the hydrogenation of p-CNB on the Au/P[ClVBTA]-M systems are summarized in Figure4. The activity of all catalysts changed with the support used. Pseudo-first-order kinetic profiles are observed for p-CNB hydrogenation in all cases as shown in Scheme 1. For all catalysts, other side-reactions as dehalogenation, deamination, and/or hydroxylation were not detected. The Au/P[VBTACl]-Al and Au/P[VBTACl]-Zr systems showed considerably higher catalytic activity than Au/P[VBTACl]-Ti at similar metal loadings. Differences in catalytic activity are related to the Au-NPs size of Au/P[VBTACl]-Al and Au/P[VBTACl]-Zr samples as evidenced from TEM and DRUV-vis characterizations. These two systems also showed higher chemoselectivity to -NO2 hydrogenation (≥99%), producing p-chloroaniline (p-CAN) as main product as shown in Table 3.Table 3
Catalytic properties for the hydrogenation of CNB isomers over Au/P[BVTACl]-M catalysts. Reaction conditions: solvent, 25 mL absolute ethanol; temperature, 298 K; stirring rate, 800 rpm; CNB isomers, 0.02 mol L−1; H2 pressure, 20 bar.
Catalyst
X
a (±0.2%)
Y
i
e
l
d
b (±1%)
TOF(min−1)
Au/P[VBTACl]-Al
83.9
100
252
Au/P[VBTACl]-Ti
42.0
98
c
49
Au/P[VBTACl]-Zr
67.4
100
99
C
o
n
v
e
r
s
i
o
n
a level at 360 minutes. Yieldb mean values. Nc-(p-chlorophenyl)hydroxylamine-intermediary was the only byproduct detected.Scheme 1
Resumed reaction pathway for the hydrogenation of p-CNB.Figure 4
Activity curves based on p-CNB conversion for all the synthesized catalysts. Dash line: pseudo-first kinetic model. Reaction conditions: CNB concentration: 0.02 mol L−1, catalyst mass: 0.050 g, PH2: 20 bar, mixing speed: 800 rpm, and solvent: absolute ethanol.The Au/P[VBTACl]-Ti system showed the lowest catalytic activity and slightly lower yields (96–98%) for the production of p-CAN where the N-(p-chlorophenyl)hydroxylamine-intermediary (NCPH) was the only byproduct detected. The presence of both segregated TiO2-anatase oxide detected by DRUV-vis and bigger Au-NPs (see Table1) could cause the incomplete hydrogenation of the NCPH-intermediary, decreasing yields of p-CAN. [20].


#### 3.2.2. p-CNB Recycling Experiment

The recyclability of the catalysts has been tested in p-CNB hydrogenation reaction. The p-CNB isomer showed the best activity-selectivity results of all catalytic reactions studied. Figure5 shows the recyclability of Au/P[VBTACl]-M catalysts in terms of activity and selectivity in five successive batches. Figure 5(a) displays the maximum conversion level for all catalysts during the different cycles at 360 minutes. The Au/P[VBTACl]-Al system used in the first run was recovered from the reaction mixture and reused in five catalytic cycles, showing a nonappreciable decline in its activity and selectivity. After the fourth cycle, total conversion had decreased by 83%. XPS measurements of the Au 4f7/2 (Table 4) in conjunction with postreaction TEM characterization (see Figure 6(a)) performed on the recovered Au/P[VBTACl]-Al system after the last run do not show BE changes nor any significative differences in Au-NPs size distribution compared to pristine sample, thus indicating that the chemical and electronic structure of the catalyst were not modified by the catalytic process. The decrease in activity in the last run could be attributed to slight leaching of the Au-NPs as was detected by ICP analysis.Table 4
ICP-AES, TEM mean Au sizes, XPS data after reaction, and TOF in the last cycle of Au/P[BVTACl]-M catalysts in the p-CNB hydrogenation. Reactions conditions: solvent, 25 mL absolute ethanol; temperature, 298 K; stirring rate, 800 rpm; substrate concentration, 0.02 mol L−1; H2 pressure, 20 bar.
Catalyst
ICP-AES(Au%)
d
T
E
M (nm)
Au 4f7/2 (eV)
Au/Msup
T
O
F
a (min−1)
Au/P[VBTACl]-Al
0.40
5.3
±
2.4
84.2
0.0040
241
Au/P[VBTACl]-Ti
0.22
17.5
±
5.3
83.8
0.0008
15
Au/P[VBTACl]-Zr
0.09
4.0
±
2.9
84.0
0.0013
7
b
T
h
e
a turnover frequency was defined at 20% of conversion for the last cycle. The values for surface metallic were determinate employing the ICP metal content and metallic dispersion after the last run. 4b% of conversion level was detected.Figure 5
Conversion level (a) and selectivity (b) versus number of reaction cycles during the m-CNB hydrogenation over Au/P[VBTACl]/M catalysts. Reaction conditions: p-CNB concentration: 0.02 mol L−1, catalyst mass: 0.070 g, PH2: 20 bar, stirring speed: 800 rpm, solvent: absolute ethanol. N-(p-chlorophenyl)hydroxylamine-intermediary was the only byproduct detected.
(a)
(b)Figure 6
Representative TEM Micrograph for Au/P[VBTACl]/M catalysts after five recycles. (a) M: Al; (b) M: Ti; (c) M: Zr.
(a)
(b)
(c)The Au/P[VBTACl]-Ti catalyst showed a significant decrease in catalytic activity during the five catalytic cycles. The drop in conversion between the first two batches is ~20%, but on the third cycle there is a drastic drop of >45%. To gain an insight into the possible mechanism causing the loss in activity and selectivity, the final catalyst has been subjected to ICP and TEM characterization as shown in Table4.After the fifth cycle Au Nps increased in size to 13–30 nm. The hydrogenation of nitroarenes catalyzed by gold-catalysts is a structure-sensitive reaction in ethanolic solution as was reported in our previous reports [19, 20, 46]. The presence of bigger Au-NPs crystallites promotes the catalysts deactivation, increasing the incomplete hydrogenation pathways. In this catalyst, NCPH was the only intermediate detected. Furthermore, a decrease in Au loading in the last run was detected by ICP analysis (~15%). Both effects contribute in the decrease of the catalytic activity. Finally, after its use in the last batch, the Au/P[VBTACl]-Ti showed that the BE of Au 4f7/2 was 83.8 eV, which is smaller than that measured on the fresh catalyst (BE 84.2 eV). This value is typical in electron-rich Au-Nps that are having strong interactions with TiO2. This effect was also reported in our previous studies of Au/TiO2-anatase catalysts [20].Finally, Au/P[VBTACl]-Zr showed a different behavior during the recycling experiments. This catalyst could not be reused with the same activity. However, in the case of p-CNB, Au/P[VBTACl]-ZrO2 showed the highest selectivity in all the cycles, which was also observed in the fresh catalyst as shown in Figure6(c). The ICP analysis showed about 22% of Au content in the final recovered catalyst; namely, about 78% of Au was leached into the reaction solvent, and this is the reason for the decreases in activity. Table 4 shows the TEM measurements for the Au/P[VBTACl]-Zr catalyst after the fifth cycle. The remaining Au nanoparticles did not show any representative aggregation after five cycles.


## 3.1. Au Nanoparticles Synthesis and Catalyst Characterization

In the catalysts synthesis, the supports were contacted with metal precursor dissolved in aqueous solution to sorb the active phase on the polymer/metal oxide surface. The HAuCl4 can exchange the chloride ligand with hydroxyl anion providing the formation of mixed chlorohydroxy complexes AuCl4-xOHx- as has been reported by Murphy and LaGrange [41]. In other way, P[VBTACl]-M hybrid systems can accumulate gold by ion-exchange process from (1) the poly-cationic quaternary ammonium pending group and (2) metal oxide surface sorption (especially in an acidic range of pH) [41]. The pH measurements could be used to examine the formation of the Au-Nps by spontaneous reduction of metal precursor on the support hybrid materials. Figure 1 shows the plot of pH versus time during the Au-NPs deposition. During the process we observed the change of solution from yellow (typical for HAuCl4 in solution) to purple as a consequence of the gold nanoparticles surface plasmon band [9, 42, 43]. All the composites show a continuous increase in the pH of the solution over time. The initial pH is 3.32 at room temperature for all the composites, though it increases during the course of the preparation to ca. 5.10, 4.58, and 4.80 for P[VBTACl]-Al, P[VBTACl]-Ti, and P[VBTACl]-Zr, respectively.Figure 1
pH versus time for P[VBTACl]/M catalyst synthesis. Conditions: gold (III) chloride hydrate precursor concentration 6.02 × 10−4 mol L−1. Temperature: 298 K and magnetic agitation: 300 rpm. The blank corresponds to the solution of precursor without the support.At the initial pH, the predominant gold species present in the solution are [AuCl3OH]− and [AuCl2(OH)2]−. The reduction of these gold chlorohydroxy complexes proceeds because they possess a minor redox potential compared to [AuCl4]−. The sorption of these species could occur in defect sites of the metal oxide surface. These defect sites could provide electronic transfer from the defects on the surface to the AuCl4-xOHx- species causing gold spontaneous reduction and thus an increase of the pH [33, 37, 38, 44]. This defects are potentials sites for reduction due certainly to the remaining free radicals initiator still trapped into the polymer/metal oxide core as was reported by Féral-Martin et al. [34].Table1 displays the ICP-AES analysis for all the Au catalysts synthesized. The Au metal content is very similar to the nominal one. The specific SBET areas are also summarized in Table 1. These values are similar to the ones of our previous results [40] and they indicate that the supports are not modified upon the impregnation procedure.Table 1
S
B
E
T, Au content, and average Au-NPs size by TEM characterization of Au/P[VBTACl]-M catalysts.
M
S
B
E
T (m2g−1)
ICP-AES(Au%)
d
p (nm)
D
i
s
p
e
r
s
i
o
n
a (%)
Al
11
0.45
5.1
±
2.7
19.5
Ti
9
0.38
10.1
±
3.8
9.9
Zr
10
0.42
4.5
±
2.5
22.2
A
s
s
u
m
i
n
g
a Au homodispersion and the same metal particle size (dp), Au dispersion was calculated using formula D%=1/dTEM×100% [19].Figure2 shows representative TEM images performed to determine the particle size of Au-NPs on the composites reported here. For the Au/P[VBTACl]-Zr and Au/P[VBTACl]-Al catalysts no significant differences in their images are observed. The active phase is randomly dispersed on the composite surface, with metal-particle aggregates particularly visible. Their size distribution is broad but finite ranging from 2.0 up to 10 nm (Figures 2(a) and 2(c)).Figure 2
Representative TEM Micrograph and Au nanoparticle size distribution measurements for Au/P[VBTACl]/M catalysts. (a) M: Al; (b) M: Ti; (c) M: Zr.
(a)
(b)
(c)The Au-NPs supported on P[VBTACl]-Ti feature a more random morphology and particle size distribution, composed of bigger crumb-like crystallites, indicative of low dispersion of Au, and the majority of the particles are in the fraction of 8.0–15 nm. On the other hand, solid structures were detected in this catalyst and were attributed to the segregation of the TiO2 phase as was informed in our previous reports [40].Curiously, P[VBTACl]-Ti was the only one to show a visible inorganic phase segregation after the hybrids synthesis. This behavior could be explained by the fast and spontaneous poly-condensation of the inorganic precursor during the sol-gel synthesis in comparison to Zr and Al metal-alkoxide precursor [45]. The Au-NPs deposited on the support surface showed a preferential deposition around the segregated TiO2-phase as was detected by TEM photographs (Figure 2(b)). On this way, TiO2 could promote a fast reduction of gold ions due to strong binding interactions with oxygen vacancies as was reported by Pan and Xu [38].DRUV-vis spectra of the catalysts are shown in Figure3. For all the Au/P[VBTACl]-M catalysts, an absorption band between 200 and 300 nm was observed. The intensity of the absorption band could be attributed to polymeric phase absorption (π→π∗ transition from benzene pending groups moieties). For Au/P[VBTACl]-Ti catalyst, TiO2 species were detected in the range 330–340 nm, indicating the presence of anatase-phase (with particle size > 5.0 nm) [46] in agreement with TEM and XRD characterization previously reported by Campos et al. [40].Figure 3
DRUV-vis spectra of the Au/P[VBTACl]/M catalyst.The plasmon of Au was observed to be centered between 530 and 560 nm, which indicates that the Au NPs are mostly spherical [47]. The intensity of the plasmon also depends on the particle size [48]. Our results are consistent with a supported metallic Au for all the catalysts where the differences in characteristic wavelength may be the result of differences in Au particle size as was discussed in TEM characterization (see Table 1).In order to get a better knowledge on the active gold state, the Au/P[VBTACl]/M catalysts were characterized by XPS as shown in Table2. Differences in Au 4f7/2 binding energy between the samples were observed. The binding energy (BE) of Au for all catalytic systems showed that Au 4f7/2 appears at 84.0–84.2 eV. This is indicative of the complete reduction of the gold precursor by the hybrid support. This could be attributed to the fact that their BE is close to that reported for metallic Au nanoparticles [21, 29]. The N 1s BE contribution was detected at 404.0–403.9 eV, which is typical for ammonium quaternary groups, while the Cl 2p3/2 at 199.3 eV corresponds to chloride counter ion in agreement with previous reported results by Deng et al. [49].Table 2
Binding energies (eV) of internal electrons and atomic surface ratio of Au/P[VBTACl]-M catalysts.
M
M2p, 3d(eV)
Au 4f7/2 (eV)
N 1s(eV)
Cl 2p3/2 (eV)
Au/Msup
N/Clsup
Al
74.6
84.2
404.0
199.1
0.0102
0.914
Ti
458.6
84.1
403.9
199.0
0.0059
0.814
Zr
182.2
84.0
404.1
199.1
0.0133
1.014The Au/M atom ratio showed a reasonable value for high Au-NPs dispersion for Au/P[VBTACl]-Al and Au/P[VBTACl]-Zr catalysts. Furthermore, Au/P[VBTACl]-Ti system showed a lower Au/Ti atom ratio, which could be attributed to a decrease in the dispersion of Au active phase and consequently an increase in the Au particle size. This shows good agreement with TEM results (see Figure2). Finally, all systems showed N/Cl atom surface ratio close to 1, which indicated that the chloride excess was successfully eliminated from catalyst surfaces (N+cation/Cl-anion).


## 3.2. Catalytic Hydrogenation Reaction

### 3.2.1. P-CNB Hydrogenation

The results obtained for the hydrogenation of p-CNB on the Au/P[ClVBTA]-M systems are summarized in Figure4. The activity of all catalysts changed with the support used. Pseudo-first-order kinetic profiles are observed for p-CNB hydrogenation in all cases as shown in Scheme 1. For all catalysts, other side-reactions as dehalogenation, deamination, and/or hydroxylation were not detected. The Au/P[VBTACl]-Al and Au/P[VBTACl]-Zr systems showed considerably higher catalytic activity than Au/P[VBTACl]-Ti at similar metal loadings. Differences in catalytic activity are related to the Au-NPs size of Au/P[VBTACl]-Al and Au/P[VBTACl]-Zr samples as evidenced from TEM and DRUV-vis characterizations. These two systems also showed higher chemoselectivity to -NO2 hydrogenation (≥99%), producing p-chloroaniline (p-CAN) as main product as shown in Table 3.Table 3
Catalytic properties for the hydrogenation of CNB isomers over Au/P[BVTACl]-M catalysts. Reaction conditions: solvent, 25 mL absolute ethanol; temperature, 298 K; stirring rate, 800 rpm; CNB isomers, 0.02 mol L−1; H2 pressure, 20 bar.
Catalyst
X
a (±0.2%)
Y
i
e
l
d
b (±1%)
TOF(min−1)
Au/P[VBTACl]-Al
83.9
100
252
Au/P[VBTACl]-Ti
42.0
98
c
49
Au/P[VBTACl]-Zr
67.4
100
99
C
o
n
v
e
r
s
i
o
n
a level at 360 minutes. Yieldb mean values. Nc-(p-chlorophenyl)hydroxylamine-intermediary was the only byproduct detected.Scheme 1
Resumed reaction pathway for the hydrogenation of p-CNB.Figure 4
Activity curves based on p-CNB conversion for all the synthesized catalysts. Dash line: pseudo-first kinetic model. Reaction conditions: CNB concentration: 0.02 mol L−1, catalyst mass: 0.050 g, PH2: 20 bar, mixing speed: 800 rpm, and solvent: absolute ethanol.The Au/P[VBTACl]-Ti system showed the lowest catalytic activity and slightly lower yields (96–98%) for the production of p-CAN where the N-(p-chlorophenyl)hydroxylamine-intermediary (NCPH) was the only byproduct detected. The presence of both segregated TiO2-anatase oxide detected by DRUV-vis and bigger Au-NPs (see Table1) could cause the incomplete hydrogenation of the NCPH-intermediary, decreasing yields of p-CAN. [20].


### 3.2.2. p-CNB Recycling Experiment

The recyclability of the catalysts has been tested in p-CNB hydrogenation reaction. The p-CNB isomer showed the best activity-selectivity results of all catalytic reactions studied. Figure5 shows the recyclability of Au/P[VBTACl]-M catalysts in terms of activity and selectivity in five successive batches. Figure 5(a) displays the maximum conversion level for all catalysts during the different cycles at 360 minutes. The Au/P[VBTACl]-Al system used in the first run was recovered from the reaction mixture and reused in five catalytic cycles, showing a nonappreciable decline in its activity and selectivity. After the fourth cycle, total conversion had decreased by 83%. XPS measurements of the Au 4f7/2 (Table 4) in conjunction with postreaction TEM characterization (see Figure 6(a)) performed on the recovered Au/P[VBTACl]-Al system after the last run do not show BE changes nor any significative differences in Au-NPs size distribution compared to pristine sample, thus indicating that the chemical and electronic structure of the catalyst were not modified by the catalytic process. The decrease in activity in the last run could be attributed to slight leaching of the Au-NPs as was detected by ICP analysis.Table 4
ICP-AES, TEM mean Au sizes, XPS data after reaction, and TOF in the last cycle of Au/P[BVTACl]-M catalysts in the p-CNB hydrogenation. Reactions conditions: solvent, 25 mL absolute ethanol; temperature, 298 K; stirring rate, 800 rpm; substrate concentration, 0.02 mol L−1; H2 pressure, 20 bar.
Catalyst
ICP-AES(Au%)
d
T
E
M (nm)
Au 4f7/2 (eV)
Au/Msup
T
O
F
a (min−1)
Au/P[VBTACl]-Al
0.40
5.3
±
2.4
84.2
0.0040
241
Au/P[VBTACl]-Ti
0.22
17.5
±
5.3
83.8
0.0008
15
Au/P[VBTACl]-Zr
0.09
4.0
±
2.9
84.0
0.0013
7
b
T
h
e
a turnover frequency was defined at 20% of conversion for the last cycle. The values for surface metallic were determinate employing the ICP metal content and metallic dispersion after the last run. 4b% of conversion level was detected.Figure 5
Conversion level (a) and selectivity (b) versus number of reaction cycles during the m-CNB hydrogenation over Au/P[VBTACl]/M catalysts. Reaction conditions: p-CNB concentration: 0.02 mol L−1, catalyst mass: 0.070 g, PH2: 20 bar, stirring speed: 800 rpm, solvent: absolute ethanol. N-(p-chlorophenyl)hydroxylamine-intermediary was the only byproduct detected.
(a)
(b)Figure 6
Representative TEM Micrograph for Au/P[VBTACl]/M catalysts after five recycles. (a) M: Al; (b) M: Ti; (c) M: Zr.
(a)
(b)
(c)The Au/P[VBTACl]-Ti catalyst showed a significant decrease in catalytic activity during the five catalytic cycles. The drop in conversion between the first two batches is ~20%, but on the third cycle there is a drastic drop of >45%. To gain an insight into the possible mechanism causing the loss in activity and selectivity, the final catalyst has been subjected to ICP and TEM characterization as shown in Table4.After the fifth cycle Au Nps increased in size to 13–30 nm. The hydrogenation of nitroarenes catalyzed by gold-catalysts is a structure-sensitive reaction in ethanolic solution as was reported in our previous reports [19, 20, 46]. The presence of bigger Au-NPs crystallites promotes the catalysts deactivation, increasing the incomplete hydrogenation pathways. In this catalyst, NCPH was the only intermediate detected. Furthermore, a decrease in Au loading in the last run was detected by ICP analysis (~15%). Both effects contribute in the decrease of the catalytic activity. Finally, after its use in the last batch, the Au/P[VBTACl]-Ti showed that the BE of Au 4f7/2 was 83.8 eV, which is smaller than that measured on the fresh catalyst (BE 84.2 eV). This value is typical in electron-rich Au-Nps that are having strong interactions with TiO2. This effect was also reported in our previous studies of Au/TiO2-anatase catalysts [20].Finally, Au/P[VBTACl]-Zr showed a different behavior during the recycling experiments. This catalyst could not be reused with the same activity. However, in the case of p-CNB, Au/P[VBTACl]-ZrO2 showed the highest selectivity in all the cycles, which was also observed in the fresh catalyst as shown in Figure6(c). The ICP analysis showed about 22% of Au content in the final recovered catalyst; namely, about 78% of Au was leached into the reaction solvent, and this is the reason for the decreases in activity. Table 4 shows the TEM measurements for the Au/P[VBTACl]-Zr catalyst after the fifth cycle. The remaining Au nanoparticles did not show any representative aggregation after five cycles.


## 3.2.1. P-CNB Hydrogenation

The results obtained for the hydrogenation of p-CNB on the Au/P[ClVBTA]-M systems are summarized in Figure4. The activity of all catalysts changed with the support used. Pseudo-first-order kinetic profiles are observed for p-CNB hydrogenation in all cases as shown in Scheme 1. For all catalysts, other side-reactions as dehalogenation, deamination, and/or hydroxylation were not detected. The Au/P[VBTACl]-Al and Au/P[VBTACl]-Zr systems showed considerably higher catalytic activity than Au/P[VBTACl]-Ti at similar metal loadings. Differences in catalytic activity are related to the Au-NPs size of Au/P[VBTACl]-Al and Au/P[VBTACl]-Zr samples as evidenced from TEM and DRUV-vis characterizations. These two systems also showed higher chemoselectivity to -NO2 hydrogenation (≥99%), producing p-chloroaniline (p-CAN) as main product as shown in Table 3.Table 3
Catalytic properties for the hydrogenation of CNB isomers over Au/P[BVTACl]-M catalysts. Reaction conditions: solvent, 25 mL absolute ethanol; temperature, 298 K; stirring rate, 800 rpm; CNB isomers, 0.02 mol L−1; H2 pressure, 20 bar.
Catalyst
X
a (±0.2%)
Y
i
e
l
d
b (±1%)
TOF(min−1)
Au/P[VBTACl]-Al
83.9
100
252
Au/P[VBTACl]-Ti
42.0
98
c
49
Au/P[VBTACl]-Zr
67.4
100
99
C
o
n
v
e
r
s
i
o
n
a level at 360 minutes. Yieldb mean values. Nc-(p-chlorophenyl)hydroxylamine-intermediary was the only byproduct detected.Scheme 1
Resumed reaction pathway for the hydrogenation of p-CNB.Figure 4
Activity curves based on p-CNB conversion for all the synthesized catalysts. Dash line: pseudo-first kinetic model. Reaction conditions: CNB concentration: 0.02 mol L−1, catalyst mass: 0.050 g, PH2: 20 bar, mixing speed: 800 rpm, and solvent: absolute ethanol.The Au/P[VBTACl]-Ti system showed the lowest catalytic activity and slightly lower yields (96–98%) for the production of p-CAN where the N-(p-chlorophenyl)hydroxylamine-intermediary (NCPH) was the only byproduct detected. The presence of both segregated TiO2-anatase oxide detected by DRUV-vis and bigger Au-NPs (see Table1) could cause the incomplete hydrogenation of the NCPH-intermediary, decreasing yields of p-CAN. [20].


## 3.2.2. p-CNB Recycling Experiment

The recyclability of the catalysts has been tested in p-CNB hydrogenation reaction. The p-CNB isomer showed the best activity-selectivity results of all catalytic reactions studied. Figure5 shows the recyclability of Au/P[VBTACl]-M catalysts in terms of activity and selectivity in five successive batches. Figure 5(a) displays the maximum conversion level for all catalysts during the different cycles at 360 minutes. The Au/P[VBTACl]-Al system used in the first run was recovered from the reaction mixture and reused in five catalytic cycles, showing a nonappreciable decline in its activity and selectivity. After the fourth cycle, total conversion had decreased by 83%. XPS measurements of the Au 4f7/2 (Table 4) in conjunction with postreaction TEM characterization (see Figure 6(a)) performed on the recovered Au/P[VBTACl]-Al system after the last run do not show BE changes nor any significative differences in Au-NPs size distribution compared to pristine sample, thus indicating that the chemical and electronic structure of the catalyst were not modified by the catalytic process. The decrease in activity in the last run could be attributed to slight leaching of the Au-NPs as was detected by ICP analysis.Table 4
ICP-AES, TEM mean Au sizes, XPS data after reaction, and TOF in the last cycle of Au/P[BVTACl]-M catalysts in the p-CNB hydrogenation. Reactions conditions: solvent, 25 mL absolute ethanol; temperature, 298 K; stirring rate, 800 rpm; substrate concentration, 0.02 mol L−1; H2 pressure, 20 bar.
Catalyst
ICP-AES(Au%)
d
T
E
M (nm)
Au 4f7/2 (eV)
Au/Msup
T
O
F
a (min−1)
Au/P[VBTACl]-Al
0.40
5.3
±
2.4
84.2
0.0040
241
Au/P[VBTACl]-Ti
0.22
17.5
±
5.3
83.8
0.0008
15
Au/P[VBTACl]-Zr
0.09
4.0
±
2.9
84.0
0.0013
7
b
T
h
e
a turnover frequency was defined at 20% of conversion for the last cycle. The values for surface metallic were determinate employing the ICP metal content and metallic dispersion after the last run. 4b% of conversion level was detected.Figure 5
Conversion level (a) and selectivity (b) versus number of reaction cycles during the m-CNB hydrogenation over Au/P[VBTACl]/M catalysts. Reaction conditions: p-CNB concentration: 0.02 mol L−1, catalyst mass: 0.070 g, PH2: 20 bar, stirring speed: 800 rpm, solvent: absolute ethanol. N-(p-chlorophenyl)hydroxylamine-intermediary was the only byproduct detected.
(a)
(b)Figure 6
Representative TEM Micrograph for Au/P[VBTACl]/M catalysts after five recycles. (a) M: Al; (b) M: Ti; (c) M: Zr.
(a)
(b)
(c)The Au/P[VBTACl]-Ti catalyst showed a significant decrease in catalytic activity during the five catalytic cycles. The drop in conversion between the first two batches is ~20%, but on the third cycle there is a drastic drop of >45%. To gain an insight into the possible mechanism causing the loss in activity and selectivity, the final catalyst has been subjected to ICP and TEM characterization as shown in Table4.After the fifth cycle Au Nps increased in size to 13–30 nm. The hydrogenation of nitroarenes catalyzed by gold-catalysts is a structure-sensitive reaction in ethanolic solution as was reported in our previous reports [19, 20, 46]. The presence of bigger Au-NPs crystallites promotes the catalysts deactivation, increasing the incomplete hydrogenation pathways. In this catalyst, NCPH was the only intermediate detected. Furthermore, a decrease in Au loading in the last run was detected by ICP analysis (~15%). Both effects contribute in the decrease of the catalytic activity. Finally, after its use in the last batch, the Au/P[VBTACl]-Ti showed that the BE of Au 4f7/2 was 83.8 eV, which is smaller than that measured on the fresh catalyst (BE 84.2 eV). This value is typical in electron-rich Au-Nps that are having strong interactions with TiO2. This effect was also reported in our previous studies of Au/TiO2-anatase catalysts [20].Finally, Au/P[VBTACl]-Zr showed a different behavior during the recycling experiments. This catalyst could not be reused with the same activity. However, in the case of p-CNB, Au/P[VBTACl]-ZrO2 showed the highest selectivity in all the cycles, which was also observed in the fresh catalyst as shown in Figure6(c). The ICP analysis showed about 22% of Au content in the final recovered catalyst; namely, about 78% of Au was leached into the reaction solvent, and this is the reason for the decreases in activity. Table 4 shows the TEM measurements for the Au/P[VBTACl]-Zr catalyst after the fifth cycle. The remaining Au nanoparticles did not show any representative aggregation after five cycles.


## 4. Conclusions

Novel Au catalysts were synthesized by an ion-exchange process and in situ spontaneous gold reduction by the polymer-metal oxide hybrid material used as support. The three metal oxides aluminum, titanium, and zirconium in the support structure showed the ability to reduce the gold precursor providing active and chemoselective catalysts for the liquid-phase hydrogenation of p-chloronitrobenzene. The most active and selective catalyst was the gold supported in the hybrid carrier with aluminum oxide as inorganic phase. The catalyst stability when recycling it depends of the metal oxide in the support structure and the maximum conversion levels follow the tendency: aluminum oxide > titanium oxide > zirconium oxide after five cycles. Finally, the gold catalyst supported on polymer/aluminum oxide can be recycled and reused at least five times without loss in activity and chemoselectivity to -NO2 group hydrogenation to produce p-chloroaniline as the main product.



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*Source: 7941853-2017-03-22.xml*