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Hydrogen Peroxide Oxidation of Aromatic Hydrocarbons by Immobilized Iron(III)

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Hydrogen Peroxide Oxidation of Aromatic Hydrocarbons by Immobilized Iron(III) Journal of Molecular Catalysis A: Chemical 217 (2004) 161–164 Hydrogen peroxide oxidation of aromatic hydrocarbons by immobilized iron(III) Hassan Hosseini Monfared∗, Zahra Amouei Department of Chemistry, School of Sciences, Zanjan University, Zanjan 45195-313, Iran Received 30 October 2003; received in revised form 16 March 2004; accepted 16 March 2004 Available online 27 April 2004 Abstract Supported iron(III) ions on neutral ␥-alumina are an efficient catalyst for the oxidation of aromatic hydrocarbons with hydrogen peroxide in acetonitrile at 60 ◦C. The catalyst is active in the low temperatue liquid phase oxidation of benzene, toluene, chlorobenzene, p-xylene, mesitylene, benzaldehyde with hydrogen peroxide. Conversions of 31–88% with respect to starting substrate were obtained within 6 h. Oxidation on both the side chain and the aromatic ring of hydrocarbons occurred. © 2004 Elsevier B.V. All rights reserved. Keywords: Aromatic hydrocarbons; Hydrogen peroxide; Heterogeneous catalyst; Oxidation 1. Introduction ions on silica [4] or alumina [5], considerably retards the non-productive decomposition of H2O2. Here, we report that The selective catalytic oxidation of organic molecules supported iron ions on ␥-alumina show remarkable catalytic continues to be a very important method for the prepara- properties in activation of H2O2 for aromatic hydrocarbons tion of primary and specialty chemicals in the chemical oxidation. industry worldwide. Catalytic oxidation reactions using metal complexes are valuable for facilitation the devel- opment of ‘no-waste’ chemical technology based on the 2. Experimental ‘atom economy’ principle [1,2]. The main driving force for the development of new efficient oxygenation cata- 2.1. Equipment lysts is the necessity to functionalize feedstock alkanes to raw oxygen-containing chemicals and the ability to selec- The reaction products were separated and identified with tively hydroxylate non-activated C–H bonds in elaborate a Hewlett-Packard 6890 Series gas chromatograph equipped chemicals in order to save many steps in the preparation with a HP-1 capillary column (methyl siloxane 30.0m × of fine chemicals. In addition, for obvious environmen- 250 ␮m×0.25 ␮m) and gas chromatograph–mass spectrom- tal constraints, classical stoichiometric oxidants, such as etry (Hewlett-Packard 5973 Series MS-HP gas chromato- dichromate or permanganate, should be replaced by new en- graph with a mass-selective detector). 1H NMR spectra were vironment friendly catalytic processes using clean oxidants recorded by use of a Bruker 500 MHz spectrometer. Atomic like molecular oxygen or hydrogen peroxide. absorptions were measured by a Varian 220 FS spectropho- In spite of the advantages of H2O2 as a cheap and benign tometer. oxidant, its catalytic application has some limitations due to decomposition of H2O2 by traces of transition metal ions 2.2. Materials [3]. Recently, we have noticed that immobilization of iron The Al2O3 (90, active neutral, 70–230 mesh) and · ∗ Corresponding author. Tel.: +98-241-5152576; FeSO4 7H2O were purchased from Merck. Benzene and fax: +98-241-5283203. other aromatic hydrocarbons were purchased commercially E-mail address: [email protected] (H.H. Monfared). and were passed through a SiO2 column just before the 1381-1169/$ – see front matter © 2004 Elsevier B.V. All rights reserved. doi:10.1016/j.molcata.2004.03.020 162 H.H. Monfared, Z. Amouei / Journal of Molecular Catalysis A: Chemical 217 (2004) 161–164 reaction to remove oxidized impurities. Acetonitrile of the Table 1 a highest grade commercially available (Merck) was used Catalytic oxidation of benzene with hydrogen peroxide without further purification. Hydrogen peroxide (35% in wa- Run Catalyst Oxidant Product yield (%) ter) was purchased from Fluka and its concentration (11.4 M) 1 None H2O2 No product was determined according to the standard procedure [6]. 2Al2O3 H2O2 No product b 3 FeSO4 H2O2 No product 3+ 2.3. Preparation of catalyst 4Fe-Al2O3 None No product 3+ 5Fe-Al2O3 H2O2 Phenol (27) 3+ a Fe -Al2O3 catalyst was prepared according to the pro- Catalyst, 0.20 g; benzene, 1.46 mmol; CH3CN, 4 ml; H2O2 (35% in T = ◦ t = cedure described previously [5] and the iron loading was de- H2O), 13.68 mmol; 60 C; and 6h. b FeSO , 0.042 mmol. termined by measuring the amount of unloaded FeSO4 in the 4 solvent and the washings by atomic absorption spectroscopy (0.210 mmol FeSO4/1 g Al2O3). Normally, the catalyst was used without any pretreatment. product is observed (Table 1, run 3). Interestingly, the sup- ported iron(III) ions almost do not catalyze non-productive 2.4. Oxidation of benzene; general procedure hydrogen peroxide decomposition but activate it for oxygen transfer to aromatic compound (Table 1, run 5). These re- 3+ Oxidation reactions were performed in a stirred round sults prove that catalytic activity of Fe -Al2O3 is due to 3+ bottom flask fitted with a water-cooled condenser. Reactions Fe . Large reduction in H2O2 decomposition by the sup- were carried out under atmospheric pressure in air in an oil ported iron(III) is to site isolation. The active centers for ◦ bath at 60 ± 1 C with acetonitrile as a solvent and aqueous catalytic oxygen transfer attributable are formed by isolated 3+ H2O2 (35%) as an oxidant. Typically, 0.200 g of Fe -Al2O3 iron species. Similarly, in oxidation of aromatic hydrocar- + catalyst (contain 0.042 mmol Fe3 ), benzene (1.46 mmol) bons with hydrogen peroxide over Zn, Cu, Al-layered dou- and acetonitrile (4 ml) were added to the flask. After the ble hydroxides, it has been proved that catalytically active ◦ mixture was heated to 60 C, 35% aqueous solution (1.2 ml, centers are formed by isolated copper species [9]. The clus- 13.68 mmol) of H2O2 was added. The typical reaction time tered copper ions are inactive in oxidation reaction but ac- was 6 h. After the required time, the reaction mixture was celerate the decomposition of hydrogen peroxide. filtered and the filtrate was dried with MgSO4. Products were In a similar manner to reported studies [10], in the pres- analyzed by gas chromatography, gas chromatograph–mass ence of H2O2 an adduct seems to be formed which may 1 1 spectrometry, and H NMR spectrometry. In order to check be an Al2O3-Fe(III)-η -hydroperoxide species stabilized by reproducibility each reaction was carried out twice. hydrogen bonding between the hydroperoxide ion and the oxygen atom of the alumina. Thus, supported iron(III) shows high activity for oxygenation of benzene with hydrogen per- 3. Results and discussion oxide without decomposing it. The reaction temperature affects the catalytic perfor- 3+ ◦ The catalyst Fe -Al2O3 was prepared by reaction of mance. The conversion of benzene at 30 C is only 15%. FeSO4 and Al2O3in methanol. During this reaction, the light The effect of solvents of acetonitrile, dichloromethane, green color solution of Fe(II) ion in methanol changed to yel- n-hexane, methanol, carbon tetrachloride, acetone, and low at early moments and finally after adsorption on Al2O3, ethanol on the oxidation of benzene with H2O2 in the pres- 3+ a cream colored solid was obtained. Examining the filtrate ence of Fe -Al2O3 were examined. The results of these + by sodium thiocyanate showed the presence of Fe3 ions. studies are shown in Table 2. The highest conversion and In a control experiment, the catalyst was prepared by using FeCl3 instead of FeSO4. The resulting catalyst was similarly a cream colored solid. Examination the oxidation of benzene Table 2 with H2O2 in the presence of these catalysts showed that a they have the same activity. It turned out that the adsorbed Effects of solvents on the oxidation of benzene iron ion on alumina is Fe(III) [7]. Run Solvent (dielectric H2O2 Benzene Phenol The results of preliminary experiments showed that hydro- concentration) (mmol) conversion (%) yield (%) gen peroxide in the absence of catalyst does not oxidize ben- 1CH3CN (36) 6 12 12 zene (Table 1, run 1) and that with 35% aqueous H O , the 2CH2Cl2 (8.93) 6 6 6 2 2 3 n-C H (1.91) 6 1 1 support Al O plays no catalytic role (Table 1, run 2). It has 6 6 2 3 4 CCl4 (2.2) 6 2 2 been reported that alumina catalyzes alkene epoxidation with 5CH3COCH3 (20.7) 6 33 9 anhydrous hydrogen peroxide. Alumina, however, suffers 6CH3OH (32.7) 6 27 6 deactivation by the absorption of water [8]. Homogeneous 7C2H5OH (24.3) 6 42 0 a 3+ iron(II) or iron(III) ions decompose H2O2 instantly at early Catalyst Fe -Al2O3, 0.20 g; solvent, 4 ml; benzene, 1.24 mmol; T = moments of the reaction to form oxygen, so that no oxidation 60 ◦C; and t = 6h. H.H. Monfared, Z. Amouei / Journal of Molecular Catalysis A: Chemical 217 (2004) 161–164 163 Table 3 3+ a Oxidation of various aromatic compounds by Fe -Al2O3/H2O2/CH3CN Number Substrate Conversion (%) Product yield (%) COOH CHO CHO OH 1 81 78 2 Cl Cl Cl 2 30 OH OH 16 14 OH 3 27 27 CH CHO 3 OH CH 3 4 24 CH CH 3 3 CH 3 13 11 CHO CH OH CH OH CH 2 2 3 5 23 H C CH H C CH H C CH OH H C CH 3 3 3 3 3 2 3 3 12 5 3 CH 3 CH CH OH 3 CHO 2 CH 3 6 22 OH OH 8 8 3 1 a 3+ 3+ ◦ Substrate, 1.46 mmol; Fe -Al2O3, 0.200 g (Fe , 0.042 mmol); CH3CN, 4 ml; H2O2, 13.68 mmol (1.2 ml, 11.4 M); T = 60 ± 1 C; and t = 6h. selectivity was obtained in the most polar (ε = 36) ace- catalytic system was filtered so that supported iron was tonitrile.
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