Eco-environmental synthesis of vinyl benzoate through transesterification catalyzed by Pd/C catalyst

Article abstract of DOI:10.4314/bcse.v32i2.13

The synthesis of vinyl benzoate via transesterification of vinyl acetate with benzoic acid was investigated by a carbon-supported palladium catalyst. The results showed that Pd (5 wt %)/C catalyst presented good catalytic and reusable performance instead of mercuric salts of strong acids. The conditions of the transesterification reaction for achieving high yields of vinyl benzoate were explored. The optimized conditions are as follows: reaction temperature, 80°C, reaction time, 10 h, catalyst dosage, 4.0 wt % of reactants, and benzoic acid/vinyl acetate molar ratio, 1:11, respectively, and the yield of vinyl benzoate was 85.7% with the purity of 98.3%. Meanwhile, the prepared Pd/C catalyst could be recycled five times without significant decrease in activity after separating from the product mixture, and the vinyl benzoate yield is still more than 81%. Furthermore, the eco-environmental synthetic method offers great potential for the industrial scale synthesis of vinyl benzoate.

Full text of DOI:10.4314/bcse.v32i2.13

Bull. Chem. Soc. Ethiop. 2018, 32(2), 351-359.
 2018 Chemical Society of Ethiopia and The Authors
DOI: https://dx.doi.org/10.4314/bcse.v32i2.13
ISSN 1011-3924
Printed in Ethiopia
ECO-ENVIRONMENTAL SYNTHESIS OF VINYL BENZOATE THROUGH
TRANSESTERIFICATION CATALYZED BY Pd/C CATALYST
Jun Gao*, Dongrui Guan, Dongmei Xu, Liwen Zhao, Lianzheng Zhang and Min Li
College of Chemical and Environmental Engineering, Shandong University of Science and
Technology, Qingdao 266590, China
(Received January 5, 2017; Revised April 7, 2018; Accepted April 19, 2018)
ABSTRACT. The synthesis of vinyl benzoate via transesterification of vinyl acetate with benzoic acid was
investigated by a carbon-supported palladium catalyst. The results showed that Pd (5 wt %)/C catalyst presented
good catalytic and reusable performance instead of mercuric salts of strong acids. The conditions of the
transesterification reaction for achieving high yields of vinyl benzoate were explored. The optimized conditions
are as follows: reaction temperature, 80 oC, reaction time, 10 h, catalyst dosage, 4.0 wt % of reactants, and benzoic
acid/vinyl acetate molar ratio, 1:11, respectively, and the yield of vinyl benzoate was 85.7% with the purity of
98.3%. Meanwhile, the prepared Pd/C catalyst could be recycled five times without significant decrease in activity
after separating from the product mixture, and the vinyl benzoate yield is still more than 81%. Furthermore, the
eco-environmental synthetic method offers great potential for the industrial scale synthesis of vinyl benzoate.
KEY WORDS: Vinyl benzoate, Transesterification, Vinyl acetate, Pd/C catalyst
INTRODUCTION
UV-curing technology has been developed rapidly because it can be used in a variety of
applications including biomaterials, adhesives, paints and other coatings [1-4]. However, the
reactive diluents used in UV-curable formulations include lots of toxic acrylate compounds [2-
5], which cause severe environmental pollution problem during the production process. Vinyl
benzoate can be considered as an eco-friendly alternative reactive diluent due to its unique
structural features in comparison with the previous acrylate reactive diluents.
Generally, vinyl benzoate can be prepared by two methods. One way is that vinyl benzoate
can be made by the reaction of acetylene and benzoic acid over a catalyst. The utilized catalyst
is a complex of Group VIII metal [6] or zinc acetate supported on activated carbon [7]. Another
method is that vinyl benzoate can be prepared by the acidolysis of vinyl acetate with benzoic
acid in the presence of mercuric salts of strong acids [7-10]. Compared to the acetylene route,
this method for the preparation of vinyl benzoate is much more easy [10]. The catalysts used in
the ester interchange reaction are mercuric acetate and sulfuric acid as reported in the references
[8-10]. However, the catalysts cannot be reused and have the disadvantages such as serious
corrosion of equipment, complicated separation procedures, catalyst deactivation and loss. Also,
the waste residue contains mercury which cannot be discharged directly otherwise it can cause
serious environmental pollution problems. Thus, it is of importance to explore the technology to
synthesize vinyl benzoate with a reusable catalyst instead of mercuric acetate and sulfuric acid
to avoid polluting environment. In particular, an environmentally friendly process is attractive
for industrial scale applications [11-13].
As a kind of environmental-friendly catalyst, supported palladium catalyst is applied in
various fields such as esterification [14-17], alkylation [14, 18], coupling reaction [19], and
electrooxidation [20], where the Pd-based catalysts show better catalytic activity. Zhu et al. [21]
studied the preparation of vinyl carboxylate, and simply mentioned the synthesis of vinyl
benzoate by PdCl2-NaCl/C catalyst or PdCl2-KCl/C catalyst. Liu et al. [22] reported the method
__________
*Corresponding author. E-mail: gao@sdust.edu.cn
This work is licensed under the Creative Commons Attribution 4.0 International License

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Jun Gao et al.
of synthesizing vinyl benzoate. In their work, both the preparation of the catalyst and the
synthesis of vinyl benzoate were not presented in details. Moreover, the catalyst prepared by the
patent method cannot be used in the synthesis process, because the metal palladium cannot be
loaded onto the activated carbon support well.
In this work, Pd (5 wt %)/C catalyst was prepared and used in the synthesis of vinyl
benzoate. The objective is to investigate the synthesis technology of vinyl benzoate from vinyl
acetate in the presence of Pd/C catalyst, which was explored in terms of reaction temperature,
reaction time, catalyst dosage, benzoic acid/vinyl acetate molar ratio, and the reusability of the
prepared catalyst.
EXPERIMENTAL
Materials
Palladium(II) chloride (PdCl2, >99%) and vinyl benzoate (>99%) were purchased from Tianjin
Guangfu Fine Chemical Co., Ltd. All the other chemicals (AR) used in this experiment were
commercial products and used without further purification. Deionized water was used for all the
experiments.
Catalyst preparation
The preparation of supported palladium catalyst is widely reported [23-27], most of which are
concerned with the preparation of Pd/C catalysts. In this work, the catalyst with a content of 5
wt % Pd-loading as reported in the literature [24] was prepared using H2PdCl4 solution for the
synthesis of vinyl benzoate. The activated carbon with the particle size of 350 mesh was used as
a support. It was submitted to oxidation treatments with nitric acid solution to increase the
number of oxygen-containing surface groups. After that, the carbon support was filtered out,
o
washed by deionized water until the filtrate reached neutral, and dried in an oven at 70 C for 4
h. Then the dried carbon support was suspended in deionized water for 24 h as reported by the
reference [24]. An aqueous solution of H2PdCl4 was prepared by completely dissolving
palladium chloride in concentrated hydrochloric acid, and the deionized water was added to
reach a volume of 50 mL. The suspension of carbon was added into the solution and the mixture
o
was stirred at 80 C for another 24 h. After the addition of a solution of sodium hydroxide, the
aqueous solution of formaldehyde (37 wt %) was added into the mixture to promote the
chemical reduction. Finally, the prepared catalyst was separated by filtration, washed with
deionized water for several times to eliminate the residual of chloride ion, and dried under
vacuum in an oven before used.
The prepared catalyst was characterized by BET. The N2 adsorption-desorption isotherms of
the catalyst was measured at 77 K using a Micromeritics ASAP 2020 instrument and the
o
samples were degassed at 280 C for 6 h before the measurement. As shown in Figure 1, the
isotherms of Pd/C catalyst displayed a type-IV sorption isotherm with a type H4 hysteresis loop
which reveals the mesoporous feature of this sample. The specific surface area of Pd/C catalyst
calculated by BET method was 519 m2/g.
Transesterification reaction
A 250-mL four-neck round bottom flask equipped with a reflux condenser and a magnetic stirrer
was used as the reactor for the transesterification of vinyl acetate with benzoic acid. The
weighed amounts of benzoic acid, vinyl acetate and Pd/C catalyst (SBET = 519 m2/g) were added
into the flask and heated in a water bath. The synthesis conditions such as reaction temperature,
reaction time, catalyst dosage and benzoic acid/vinyl acetate molar ratio were investigated. After
the reaction finished, the temperature of the mixture of the products and unreacted reactants
decreased slowly to the room temperature, then ethanol was added into the reaction mixture to
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Eco-environmental synthesis of vinyl benzoate through transesterification catalyzed by Pd/C 353
dissolve the organic compounds absorbed on the surface of the catalyst. The Pd/C catalyst was
separated by filtration and reused after processed in the regenerated experiment. At last, a
suitable amount of water was added into the mixture, and two phases were obtained. The upper
phase consisted of the unreacted vinyl acetate and vinyl benzoate, and the aqueous phase
consisted of acetic acid, ethanol and water. The vinyl benzoate product was separated from the
upper layer by distillation. The yield of the product (Y, %) was calculated by Y (%) = WP/WAll
×
100, where WP and WAll are the mass of product and the mass of benzoic acid, respectively. The
reaction formula for the synthesis of vinyl benzoate is shown in Scheme 1.
350
300
250
200
150
100
50
0.0
0.2
0.4
0.6
0.8
1.0
Relative Pressure / p
Figure 1. N2 adsorption/desorption isotherms of Pd/C.

p°-1
Scheme 1. Synthesis of vinyl benzoate from excess vinyl acetate and benzoic acid.
Characterization of product
The samples were characterized by NICOLET 380 FT-IR using potassium bromide tableting
method, and the infrared spectra in the range 4000–400 cm-1 were recorded. The samples were
analyzed by the gas chromatography (Lunan GC SP-6890), which was equipped with a flame
ionization detector (FID) and a capillary column (30 m × 0.25 mm × 0.5 m). High purity
nitrogen was used as carrier gas with the flow rate of 0.6 mL/min. The initial temperature of the
column was set to 373.15 K for 5 min, the final temperature was 463.15 K for 7 min, and the
heating rate was 15 K/min. The detector temperature was kept at 473.15 K, while the injection
port temperature was 383.15 K.
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RESULTS AND DISCUSSION
Characterization and analysis
The standard vinyl benzoate sample and synthesized vinyl benzoate were analyzed by FTIR as
shown in Figure 2. The main peaks are located at 3093, 1735 and 1647–1453 cm-1, which
correspond to C=C, O=C–O and substituents on benzene skeleton vibration, respectively. From
the two FT-IR spectrum curves, the absorption positions of special functional groups of the
synthesized vinyl benzoate and standard sample are consistent. Besides, 2927 and 2856 cm-1 are
saturated C–H stretching vibration region in the spectrum of products, which indicates a small
amount of vinyl acetate existed in the product.
Figure 2. FT-IR spectra of vinyl benzoate standard sample (a) and synthesized vinyl benzoate
(b).
Figure 3. Gas chromatogram of vinyl benzoate standard sample (a) and synthesized product (b).
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Eco-environmental synthesis of vinyl benzoate through transesterification catalyzed by Pd/C 355
The peak areas of all samples were determined by gas chromatography with the N2000
chromatography workstation software which was developed by Zhejiang University. According
to the retention time of the samples of pure vinyl acetate and vinyl benzoate, vinyl benzoate is
shown at the retention time of 15 min in Figure 3. The purities of the vinyl benzoate standard
sample and the vinyl benzoate product are 98.3%, 99.0%, respectively.
Effect of reaction temperature
The effect of the reaction temperature on the transesterification of vinyl acetate with benzoic
acid was explored at 50, 60, 70, 80 and 90 oC with the conditions of reaction time, 10 h, weight
ratio of catalyst to reactants, 3.0% and benzoic acid/vinyl acetate molar ratio, 1:9. As shown in
Figure 4, the vinyl benzoate yield increases from 61.2% to 82.4% as the temperature increases
from 50 oC to 80 oC. However, when the reaction temperature reaches 90 oC, the yield of vinyl
benzoate decreases obviously. Thus, the temperature used for reusability test of the prepared
catalyst is 80 oC.
Figure 4. Effect of temperature on transesterification of vinyl acetate at the reaction conditions:
reaction time, 10 h; catalyst/reactants weight ratio, 3.0% and benzoic acid/vinyl acetate
molar ratio, 1:9.
Effect of reaction time
To investigate the effect of reaction time, the reaction was carried out with the reaction time in
range of 4-12 h while the other conditions are as follows: reaction temperature, 80 oC,
catalyst/reactants weight ratio, 3.0% and benzoic acid/vinyl acetate molar ratio, 1:9. Also as
shown in Figure 5, the yield of vinyl benzoate increases from 65% to 82% with increasing
reaction time from 4 h to 10 h. But the vinyl benzoate yield decreases after the reaction time of
10 h, which could be due to the obvious reverse reaction after equilibrium condition reached.
Therefore, the appropriate reaction time is 10 h.
Effect of catalyst dosage
The reaction was carried out at five different catalyst dosages of 2.0, 2.5, 3.0, 3.5 and 4.0 wt %
of the amount of reactants while the other conditions are as follows: reaction temperature, 80 oC,
reaction time, 10 h, and benzoic acid/vinyl acetate molar ratio, 1:9. The effect of catalyst dosage
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on transesterification is shown in Figure 6. The yield of vinyl benzoate increases from 76.5% to
84.7% as the catalyst dosage increases, which indicates that the prepared catalyst can improve
the product yield, since more active sites are supplied for the transesterification reaction by the
larger catalyst dosage.
Figure 5. Effect of reaction time on transesterification of vinyl acetate at the reaction conditions:
reaction temperature, 80 oC; catalyst/reactants weight ratio, 3.0% and benzoic
acid/vinyl acetate molar ratio, 1:9.
Figure 6. Effect of catalyst dosage on transesterification of vinyl acetate at the reaction
o
conditions: reaction temperature, 80 C; reaction time, 10 h and benzoic acid/vinyl
acetate molar ratio, 1:9.
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Eco-environmental synthesis of vinyl benzoate through transesterification catalyzed by Pd/C 357
Effect of benzoic acid/vinyl acetate molar ratio
The transesterification reaction between benzoic acid and vinyl acetate is a reversible process.
To reduce the rate of reverse reaction, acetic acid should be separated continuously or excess
amount of vinyl acetate is used. However, it is not possible to remove acetic acid from this
system since the reaction temperature is not higher than the boiling temperature of acetic acid.
Therefore, the excess amount of vinyl acetate was employed in the work. The reaction was
carried out with molar ratio of benzoic acid to vinyl acetate in the range of 1:5-1:13 while the
other conditions are as follows: reaction temperature, 80 oC, reaction time, 10 h and
catalyst/reactants weight ratio, 3.0%.
As shown in Figure 7, the vinyl benzoate yield increases with increasing the molar ratio of
vinyl acetate to benzoic acid till to 11 and then decreases. The results show that a small amounts
of vinyl acetate is not favor in synthesizing vinyl benzoate, while the excess amount of vinyl
acetate could promote the equilibrium to the right hand side. Since the large amount of vinyl
acetate decreased the concentration of benzoic acid, the transesterification reaction rate
decreased, which resulted the lower product yield at the fixed reaction time of 10 h. Therefore,
considering the equilibrium conversion and economic factors, the optimized molar ratio of
benzoic acid to vinyl acetate is 1:11.
Figure 7. Effect of benzoic acid to vinyl acetate molar ratio on transesterification of vinyl acetate
at the reaction conditions: reaction temperature, 80 oC; reaction time, 10 h and
catalyst/reactants weight ratio, 3.0%.
Reusability of catalyst
To explore the reusability of the prepared catalyst, the experiments were carried out at
o
temperature of 80 C, reaction time of 10 h, catalyst dosage of 4.0 wt % of reactants and the
molar ratio of benzoic acid to vinyl acetate of 1:11, respectively. As shown in Figure 8, the
prepared catalyst has excellent reusability, since the yield of vinyl benzoate is 81% after five
times. And the catalyst could be separated from the reaction mixture without lost. Meanwhile,
its activity is stable for the transesterification.
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Figure 8. Vinyl benzoate yield vs. run number of the prepared Pd/C catalyst.
CONCLUSION
The catalyst of carbon-supported palladium was prepared for the transesterification of vinyl
acetate to synthesize vinyl benzoate. The catalyst could be easily separated from the reaction
mixture and showed better reusable performance. Furthermore, the prepared catalyst provides
more environmental friendly process than mercuric salts catalyst for the synthesis of vinyl
benzoate. The optimized conditions with the highest yield of 85.7% were obtained, and are as
follows: reaction temperature, 80 oC, reaction time, 10 h, catalyst dosage, 4.0 wt % of reactants,
benzoic acid/vinyl acetate, 1:11.
ACKNOWLEDGEMENT
The authors are thankful to the financial support of the National Natural Science Foundation of
China (Grant No. 21306106).
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