versión On-line ISSN 1996-840X
versión impresa ISSN 0379-4350
S.Afr.j.chem. (Online) vol.68 Durban 2015
Department of Chemistry, Nelson Mandela Metropolitan University, P.O. Box 77000, Port Elizabeth, 6031, South Africa
Polyvinylbenzylchloride nanofibres were fabricated by the electrospinning technique and subsequently functionalized with a tetradentate ligand, 2,2'-(1E',1'E)-(1,2-phenykenebis(azan-1-yl-1-ylidene))bis(methan-1-yl-1-ylidene)bis(4-aminophenol). VO2+ was then incorporated into the nanofibres to produce the catalyst VO-fibres. Microanalysis, TG and FT-IR were used for the characterization of VO-fibre, and EPR also confirmed the presence of oxidovanadium(IV) within the nanofibres. Oxidation of dibenzothiophene (DBT) was investigated by varying the catalyst amount, substrate amount, oxidant and temperature, and the progress of oxidation was followed with a gas chromatograph fitted with a flame ionization detector. An increase in the amount of oxidant caused an increase in the amount of dibenzothiophene sulfone (DBTO2), while a decrease in the quantity of dibenzothiophene resulted in an increase in the overall yield of dibenzothiophene sulfone under a constant temperature and oxidant (H2O2) concentration. Dibenzothiophene sulfone was confirmed as the oxidation product through 1H-NMR spectroscopy and single crystal X-ray diffraction.
Keywords: Vanadium(IV) catalyst, nanofibres, dibenzothiophene, oxidation, hydrogen peroxide (H2O2)
Fuels contain sulfur compounds in which dibenzothiophene makes up about 70 % of the sulfur content.1,2 On combustion of the fuel, sulfur oxides and other secondary airborne particulates are released to the atmosphere causing environmental and health concerns.3 These concerns have driven the need to reduce sulfur emissions to the atmosphere through the regulation of sulfur in transportation fuels.4
Currently, hydrodesulfurization (HDS) technology is being employed in the petroleum refining industries for the elimination of sulfur compounds through hydrogen reduction to H2S followed by conversion to elemental sulfur. However, the process suffers a drawback in that it does not eliminate sulfur completely due to difficulties in reducing some refractory compounds such as benzothiophene, and dibenzothiophene and its alkylated derivatives. In search for a complementary approach to the HDS, biodesulfurization (BDS) and oxidative desulfuri-zation (ODS) technologies were introduced.5-17 Bio-desulfuriza-tion involves the use of microorganisms (e.g. bacteria) to desulfurize fuels under biological processes5-10 while the ODS process involves the oxidation of the sulfur atoms followed by the extraction of the oxidation products.11-17
Several oxidants such as nitric acid and/or nitrogen oxides,11 organic hydroperoxides,12,13 peroxyacids,14,15 and hydrogen peroxide,16,17 have been employed for the catalyzed oxidation of organosulfur compounds in fuels. Studies have shown that hydrogen peroxide appears to be a promising oxidizing agent in the catalyzed oxidation of sulfur compounds in fuels due to the fact that it offers a high amount of active oxygen and produces only water as a by-product.18-25
The activity and selectivity of metal complexes immobilized on polymer microspheres have been reported in our previous studies to be as efficient as unsupported metal complexes.26-29 In an attempt to improve the surface area of the polymeric support, electropsun polymer fibres have also been reportedly employed as an alternative.30-33
This paper describes the development of oxidovanadium(IV) catalyst immobilized on 2,2'-(1E,1'E)-(1,2-phenylenebis(azan-1-yl-1-ylidene))bis(methan-1-yl-1-ylidene)bis(4-aminophenol)-PVB electrospun nanofibres for the oxidation of dibenzo-thiophene. The oxidation reaction was monitored by varying the amount of dibenzothiophene (substrate), catalyst, H2O2 and temperature.
Dibenzothiophene (99 %, Merck Chemicals, USA), 4-vinyl-benzylchloride (90 %, Sigma-Aldrich), 2,2-azobis(iso-butyronitrile) (AIBN) (98 % Sigma-Aldrich, South Africa), hydrated vanadyl sulfate [VIVOSO4.3H2O] (Sigma-Aldrich, Germany), tetrahydrofuran (THF) (99.5 %, Merck Chemical), N,N-dimethylformamide (DMF) (99 %, Merck Chemicals) and methanol (99 %, Merck Chemicals) were used as received. All other chemicals and solvents were of reagent grade.
FT-IR spectra (4000-100 cm-1) were recorded on a Bruker Tensor 27 platinum ATR-FTIR spectrometer. Microanalysis was carried out using ElementarAnalysenSystemeVario® MICRO VI 6.2 GmbH. The vanadium content was determined using a Thermo Electron (iCAP 6000 Series) inductively coupled plasma - optical emission spectrometer (ICP-OES), and wavelengths with minimum interferences were chosen (290.88 nm, 292.40 nm, 309.31 nm, and 311.07 nm). Polymer nanofibres were imaged using a TESCAN Vega TS 5136LM scanning electron microscope (SEM). Before images were taken, the fibres were coated with a thin film of gold to prevent surface charging and to protect the surface material from thermal damage by the electron beam. The BET surface area and porosity analysis for the nanofibres were performed using a Micromeritics ASAP 2020. Prior to analysis the nanofibres were degassed for 10 days at 60 °C. EPR spectra were recorded on a Bruker ESP 300E X-band spectrometer. The GC conditions were as follows: Zebron Phenomenex ZB-5MSi, capillary column (30 m x 0.25 mm x 0.25 μm), and helium was used as carrier gas at a flow rate of 1.63 mL min-1 with an average velocity of 30.16 cm sec-1 and a pressure of 63.73 KPa. The analysis run was started with an oven temperature of 80 °C ramping to 100 °C for 2 min, and then increased to 280 °C at a rate of 20 °C min-1.
2.3. Synthesis of Poly(vinylbenzylchloride) (PVBC)
The polymerization procedure was described by Fayemi and co-workers.34 A solution of 4-vinylbenzylchloride (4-VBC) (10 mL) in 2 mL of toluene was polymerized at 70 °C for 12 h in the presence of 2,2-azobis(isobutyronitrile) (0.05 g) under an argon atmosphere. The resulting brown solid was dissolved in 20 mL of THF, and the resultant solution was transferred into a beaker containing methanol, giving rise to a white polymer precipitate of PVBC. The purification of PVBC was achieved by re-dissolving PVBC in tetrahydrofuran and re-precipitating the resultant solution into methanol. The precipitate was dried under vacuum.
2.4. Fabrication and Functionalization of PVBC Nanofibres
The polymer solution for electrospinning was prepared by dissolving predetermined concentrations (50 wt%) of the polymer in DMF:THF (1:1) and gently stirred overnight at room temperature to obtain a homogeneous solution. DMF/THF was employed as the solvent of choice due to the dielectric constant they present which enhances the electro spinning of PVBC polymer. The PVBC solution was poured into a 25 mL syringe attached to a needle. The syringe needle was connected to the positive electrode of high voltage power supply. The substrate collector is an aluminum foil placed on a metallic support and connected to ground. A syringe pump (74900 series, Cole-Parmer Instrument Company, Vernon Hills, IL) was used to supply a constant flow of polymer solution from the syringe during electro-spinning process. A voltage of 18-19 kV was applied and the polymer solution flow rate used was between 0.05 and 0.1 mL h-1. Distance between the needle tip and the aluminum collector plate was 18 cm. Temperature in the fume hood during the electro-spinning process was 18±3°Cforall experiments. Nanofibres, which were collected on the aluminum foil membranes, were kept overnight in the fume-hood to allow the evaporation of solvent.
2.5. Functionalization of PVBC Nanofibres
To 1 g (0.012 mol) of 2,2'-(1E,1'E)-(1,2-phenylenebis(azan-1-yl-1-ylidene))bis(methan-1-yl-1-ylidene)bis(4-aminophenol),26 dissolved in 10 mL methanol, 1 g of PVBC nanofibres was added, and the resulting mixture was then shaken on a mechanical shaker for 48 h (Scheme 1). The functionalized nanofibres were then removed, washed with excess methanol, and then dried in air. 1gof functionalized nanofibres was soaked in a known solution (0.1 M) of VOSO4for 24 h to produce the resultant nanofibres (VO-fibres). Anal. Found (%)C=76.03;H=7.32; N=2.83;V= 0.7.
2.6. Metal Content Determination
The vanadium content in the VO-fibres (before and after use) was determined by weighing out 0.025 g of material into different vials, 10 mL of TraceSelect HNO3 (69 %) was added to each vial, the mixtures were heated up to a temperature of 40 °C for 12 h to leach out the vanadium. The acid-leached solutions were then diluted with deionized, distilled water to 100 mL and analyzed by using ICP-OES.28
2.7. Oxidation of Dibenzothiophene
The oxidation of dibenzothiophene was carried out using catalytic nanofibres in a 25 mL flask. In a typical reaction, an aqueous solution of 30 % H2O2, catalyst and dibenzothiophene in variable amount were mixed in 10 mL of methanol with continuous stirring at 250 rpm in an oil bath under various temperatures. The oxidation reaction was considered to begin on addition of the required amount of the 30 % H2O2. Progress of the reaction was monitored by using a gas chromatograph coupled to a flame ionization detector (GC-FID), by withdrawing small aliquots after specific time intervals.
3. Results and Discussion
The 2/2'-(2E/2'E)-(1,2-phenylenebis(azan-1-yl-1-ylidene))bis (methan-1-yl-1-ylidene)bis(4-aminophenol)26 functionalized nanofibres (Scheme 1) presented a low nitrogen as well as vanadium content. The low nitrogen content was also observed by Fayemi et al.34 upon functionalizing PVBC with triethylene-tetramine (TETA) and lris-(2-aminoethyl) amine (TAEA). The low nitrogen and vanadium loading could be attributed to functionalization reaction being carried out at room temperature to avoid harsh condition on the fibres.
3.2. Surface Area of PVBC and VO-fibre
Surface area measurements using carbon dioxide as adsorption gas at 273 K was carried out by using a Micrometrics ASAP 2020 surface area and porosity analyzer. The surface area of PVBC nanofibres was found to be 342 m2 g-1.34 Upon functiona-lization with 2,2'-(1E,1'E)-(1,2-phenyleneibis(azan-1-yl-1-ylidene))bis(methan-1-yl-1-ylidene)bis(4-aminophenol) and VOSO4 the polymer fibres surface area dropped to 122 m2 g-1. The reduction in surface area was due to the functionalization of PVBC on the surface.
3.3. FT-IR Spectral Studies
The disappearance of C-Cl (stretching) and CH2-Cl (bending) peaks at 678 cm-1 and 1260 cm-1 respectively for polyvinylbenzyl-chloride (PVBC) was observed upon functionalizing with 2,2'-(1E,1'E)-(1,2-phenylenebis(azan-1-yl-1-ylidene))bis(methan -1-yl-1-ylidene)bis(4-aminophenol) and VOSO4 (Fig. 1). The broad band appearing in the region 3240-3500 cm-1 and sharp bands at 1625 cm-1 were attributed to H2Oand v(C=N) (azomethine stretch) respectively, while the v(V = O) for VO-fibres appeared at 985 cm-1.26,35
3.4. Scanning Electron Micrograph (SEM) Images of Nanofibres
SEM images of electrospun polyvinylbenzylchloride nano-fibres as well as VO-fibres are presented in Fig. 2. The diameter of the fibres was in the range 0.15-0.28 μm (150-280 nm). The images show no significant change in nanofibres morphology upon functionalization of polyvinylbenzylchloride with 2,2'-(1E,1'E)-(1,2-phenyleneibis(azan-1- yl-1-ylidene)) bis(methan-1-yl-1-ylidene)bis(4-aminophenol) and VOSO4. The functionalized nanofibres were generally observed to be in the diameter range of between 0.35 and 0.58 μm (350-580 nm).
3.5. Thermo-gravimetric Analysis of VO-fibre
The thermogram of VO-fibre show that the evaporation of residual solvents (9 %) occurred up to 100 °C. The VO-fibre stability was mostly maintained between 100 °C and 200 °C with a loss of 2 % (attributed to H2O from the vanadium salt) followed by rapid decomposition of VO-fibre polymer backbone as well as the ligand, 2,2'-(1E,1'E)-(1,2-phenylenebis(azan-1-yl-1-ylidene))bis(methan-1-yl-1-ylidene)bis(4-aminophenol), with a weight loss of 74 % in a temperature range of 205-376 °C to give a vanadium oxide and carbon residue (Fig. 3).
3.6. Oxidation of Dibenzothiophene
3.6.1. Effect of Catalyst Variation The effect of catalyst variation was studied on the oxidation of dibenzothiophene and it was observed that the overall oxidation yield increased with an increase in the catalyst amount (Table 1). The catalytic activity of polymer supported vanadyl complexes was studied by varying the mass of catalyst from 20 mg (0.0223 mmol) to 100 mg (0.1115 mmol) at constant mass of dibenzothiophene 0.15 g (0.69 mmol) and hydrogen peroxide (0.008 mol) in 10 mL of methanol at 50 °C. At a catalyst mass of 100 mg the oxidation reaction yield increased to 82 % (80 % sulfone and 2 % sulfoxide) (Fig. 4). The reaction was observed to produce an overall conversion of less than 17 % in the absence of the catalyst.26 The turnover frequency (TOF) for dibenzothiophene decreased from 441 to 113 h-1 (Table 1). A plot of mass of catalyst (vanadium + support) against % conversion (Fig. 4) suggests a linear relationship but a plot of the actual moles of vanadium against % conversion showed a slight decrease in % conversion with an increase in moles of vanadium (Fig. 5), and this may be attributed to diffusion constraints when larger quantities of fibre are used.
3.6.2. Effect of Oxidant Concentration
Varying the H2O2 concentration on oxidation of dibenzo-thiophene at constant amount of dibenzothiophene (0.15 g, 0.69 mmol) and catalyst (50 mg) at 50 °C resulted in the production of a higher amount of dibenzothiophene oxides under different conditions (Table 1).
An increase in the concentration of oxidant was observed to have a positive effect on the overall yield of dibenzothiophene sulfone. At oxidant amount of 0.001 mol, an oxidation yield of 69 % was observed, upon increasing the oxidant concentration to a maximum of 0.019 mol the overall reaction yield also increased to 99 % (Fig. 6). A large amount of oxidant in the reaction mixture, however, resulted in the leaching of vanadium from the catalyst support. A much higher selectivity for dibenzothiophene sulfone in the oxidation was influenced by a higher concentration of hydrogen peroxide while more dibenzothiophene sulfoxide was produced at lower amount of oxidant (Fig. 6). The turnover frequency (TOF) of dibenzo-thiophene oxidation varied between 175 and 276 h-1 (Table 1).
3.6.3. Effect of Dibenzothiophene Concentration
The oxidation of dibenzothiophene was studied by varying its mass (mole) from 0.1 g (0.463 mmol) to 0.3 g (1.389 mmol) while a constant amount of H2O2 (0.008 mol) and catalyst (0.00167mmol) were used in the reaction mixture at 40 °C using 10 mL methanol. From the oxidation studies of dibenzothiophene, an increase in the amount of dibenzothiophene at constant amount of H2O2 and catalyst resulted in a decrease in dibenzothiophene sulfone yield. A maximum overall oxidation yield of 91.7 % (90.6 % sulfone and 1.1 % sulfoxide) was observed. The selectivity for dibenzothiophene sulfone in the oxidation system was influenced by the decrease in the concentration of dibenzothiophene and selectivity for dibenzothiophene sulfoxide was observed as the amount of dibenzothiophene was increased, and this was attributed to the low amount of oxidant available for the further oxidation of the sulfoxide when a high quantity of dibenzo-thiophene is used (Fig. 7). The turnover frequency (TOF) for the oxidation of dibenzothiophene during dibenzothiophene variation in the presence of VO-fibre catalyst varied from 168 to 389 h-1 (Table 1).
3.6.4. Effect of Temperature Variation
The oxidation reaction was studied at three different temperatures 40 °C, 55 °C and 70 °C. The rate of oxidation increased with an increase in temperature, suggesting that the reacting molecules collide more often at an elevated temperature. The selectivity for dibenzothiophene sulfone in the oxidation reaction was also influenced by the increase in the temperature and selectivity for dibenzothiophene sulfoxide was favoured by a decrease in temperature (Fig. 8). The turnover frequency (TOF) for oxidation of dibenzothiophene during the temperature variation in the presence of catalyst varied from 175 to 273 h-1 (Table 2).
3.7. EPR Studies
The presence VIVO-ligand species in VO-fibre was ascertained by EPR. The EPR spectra of VO-fibre before and after use are presented in Fig. 9. V4+ species exhibit a hyperfine structure derived from the interaction of free electrons (3d1) with the magnetic nuclear moment of 51V(7 = 7/2), and the EPR signal should split eightfold.26 The additional splitting displayed by the catalyst, VO-fibre and recycled VO-fibre, was due to the anisotropic nature of the magnetic moment of vanadyl on the polymer sup-port.36 A slightly different splitting pattern was observed on the spectrum of the recycled catalyst (Fig. 9) and was attributed to a possible change in the vanadium environment, i.e. the complex is recovered in a slightly different coordination environment. The anisotropic spectrum of VO-fibre showed g = 1.9567 and A= 161.2 x 10-4 cm-1, and the recycled VO-fibre parameters gave a g = 1.9653 and A=158.4 x 10-4 cm-1.
3.8. Catalytic Mechanism of Oxidovanadium(IV)-catalyzed Oxidation of Dibenzothiophene
UV/Vis studies showed that intermediate species were formed during the catalytic oxidation process; oxidovanadium(IV) was oxidized to dioxidovanadium(V) and oxidoperoxido species.29 The peroxo protonates to form the hydroxyl-peroxidovana-dium(V) species. Electron pairing between the sulfur atom of dibenzothiophene and an oxygen atom of the hydroxyl-peroxidovanadium(V) species resulted in bond formation therefore, giving rise to the oxidation product (Scheme 2). Dibenzothiophene sulfoxide is first formed; further oxidation resulted in the formation of dibenzothiophene sulfone (Scheme 3).
3.9. Product Analysis
126.96.36.199H-NMR and FT-IR
A white crystalline solid, dibenzothiophene sulfone, was obtained as the catalyzed oxidation product of dibenzothiophene. The oxidation product was characterized by using nuclear magnetic resonance (NMR) spectroscopy and Fourier transform infrared (FT-IR) spectroscopy. 1H-NMR δH (400 MHz, DMSO): 8.22(d, J = 7.7,2H),8.00(d, J = 7.6,2H),7.82(t, J = 7.6,2H),7.67(t, J = 7.6,2 H). FT-IR (cm-1): 1354 cm-1 u(S = o), 755 cm-1 u(C-S), 1520 cm-1 u(C=C).26,27
3.9.2. Structure Determination and Refinement of Dibenzothiophene Sulfone
Single crystals of dibenzothiophene sulfone suitable for X-ray analysis were produced on oxidation of dibenzothiophene and allowing the solvents to evaporate slowly. Intensity data were collected on a Bruker APEX II CCD diffractometer with graphite monochromated Mo Ka radiation using the APEX 2 data collection software.37 The molecular structure is presented in Fig. 10.
Crystal data and details for the determination of the structure are presented in Table 3. The structure was solved by direct methods applying SHELXS-2013 and refined by least-squares procedures using SHELXL-2013.38 The crystal structure diagram was drawn with ORTEP-3 for windows.39 The bond distances between sulfur and oxygen are quite short, hence confirming the formation of double bonds between sulfur (S) and oxygen (O) atoms. The bond distances and angles between atoms within the molecule are presented in Table 4.
3.10. Reusability Studies
The reusability of the catalyst, VO-fibre, was studied to establish the activity of the catalyst using the following conditions: [H2O2] = 0.005 mol; [catalyst] = 1.67 x10-6 mol; [dibenzothiophene] = 0.15 g (0.69 mmol); MeOH = 10 mL and temp.: 55 °C. The VO-fibre catalyst showed a decreased activity on the second and third cycles. The overall oxidation of dibenzo-thiophene for the second and third cycle was 80 % and 76 %, respectively, compared with 85 % obtained in the first cycle. The reduction in catalyst activity was attributed to the leaching of vanadium from VO-fibre, and 21 % vanadium was leached into solution after the first oxidation cycle.
The polymer nanofibres containing vanadyl ion were fabricated. EPR studies confirmed the presence of V(IV) within the polymer nanofibres and also indicated that V(V) was recycled back to V(IV) after the oxidation cycle. The catalyst, VO-fibres, showed activity towards dibenzothiophene oxidation, and the reduction in the catalyst activity after the first cycle was attributed to the leaching of vanadium from VO-fibre. VO-fibre will probably be useful under continuous flow oxidation in order to limit the catalyst leaching rather than the batch oxidation reaction procedure carried out in this account.
CCDC 1051696 contains the supplementary crystallographic data for this paper. This data can be obtained free of charge from The Cambridge Crystallographic Data Centre via www.ccdc.cam.ac.uk/data_request/cif
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Received 3 March 2015
Revised 12 June 2015
Accepted 6 July 2015