MARCEL DEKKER, INC. • 270 MADISON AVENUE • NEW YORK, NY 10016 ©2003 Marcel Dekker, Inc. All rights reserved. This material may not be used or reproduced in any form without the express written permission of Marcel Dekker, Inc. PETROLEUM SCIENCE AND TECHNOLOGY Vol. 21, Nos. 1 & 2, pp. 275–282, 2003 Green Catalytic Oxidation of Cyclohexanone to Adipic Acid Shi-gang Zhang, Heng Jiang,* Hong Gong, and Zhao-lin Sun Department of Materials Science, Fushun Petroleum Institute, Fushun, P.R. China ABSTRACT Synthesis of adipic acid by catalytic oxidation of cyclohexanone with 30% hydrogen peroxide in the presence of sodium tungstate catalyst can be well performed under reflux temperature. The adipic acid isolated yield reaches to 82.1%, and the purity of the product is also very high. The catalytic oxidation reaction takes place without any organic solvent and phase-transfer agent. The effects over different acidic ligands and the amount of the ligand on the catalytic oxidation were investigated. The catalysts exhibit high activity for the catalytic oxidation reaction of the mixture of cyclohexanone and cyclohexanol to adipic acid by 30% hydrogen peroxide under reflux temperature. *Correspondence: Heng Jiang, Department of Materials Science, Fushun Petroleum Institute, Fushun 113001, P.R. China; E-mail: hjiang78@hotmail. com. 275 DOI: 10.1081/LFT-120016948 Copyright & 2003 by Marcel Dekker, Inc. 1091-6466 (Print); 1532-2459 (Online) www.dekker.com MARCEL DEKKER, INC. • 270 MADISON AVENUE • NEW YORK, NY 10016 ©2003 Marcel Dekker, Inc. All rights reserved. This material may not be used or reproduced in any form without the express written permission of Marcel Dekker, Inc. 276 Zhang et al. Key Words: Adipic acid; Green catalytic oxidation; Cyclohexanone; Hydrogen peroxide. INTRODUCTION Adipic acid is an important chemical mainly used for manufacture of nylon-6,6, whose production is up to 2.2 million metric tons per year (Xuan, 1999). Currently the industrial production of adipic acid uses nitric acid oxidation of cyclohexanol or a tow-step oxidation of cyclohexane process by nitric acid. The nitrous oxide is the inevitable stoichiometric waste produced by this process. Despite the efforts made to decrease the emission of this waste by recovering or recycling of the nitrous oxide, about 400,000 metric tons are still emitted into the environment each year, which corresponds to 5–8% of the worldwide anthropogenic emission of N2O (Noyori et al., 1998). As it is well known that the nitrous oxides cause the ozone depletion as well as acid rain and smog which are harmful for our earth. Together with the development of the environmental legalization and the environmentally conscious of the common people, to find a new clean way to produce adipic acid has become very necessary. Many attempts have been made to substitute the classical process, such as the direct oxidation of cyclohexane to adipic acid by molecular oxygen (Schulz and Onopchenko, 1981) or by air (Park and Goroff, 1993), manufacture of adipic acid by hydrocarboxylation of pentenic acid (Denis et al., 1995; Bruner et al., 1998), and synthesis of adipic acid from biomass-derived carbon sources (Frost and Draths, 1996) or from D-glucose (Draths and Frost, 1994). But these processes would not be the ideal one because of the low yield or the terminal products are too complex for the isolation of the wanted product. Aqueous hydrogen peroxide as an ideal clean oxidant also achieves great interest. Noroyi et al., reported a practical method of oxidation cyclohexene with 30% hydrogen peroxide in presence of small amounts of Na2WO4 and [CH3(n-C8H17)3N]HSO4 as a phase transfer catalyst. A novel clean peroxy tungstate-organic complex catalyst was also used to catalyze oxidation of cyclohexene by 30% hydrogen peroxide to produce adipic acid at a high yield (Ma et al., 2001). Long chain carbon alkyl ammonium sulfate was used to substitute the expensive phrase transfer catalyst to produce adipic acid and obtained a yield of 81.7% (Gong et al., 2000). The industrial production of cyclohexene is mainly by partially hydrogenation of benzene or by dehydration of cyclohexanol. As the process needs critical conditions, the price of cyclohexene is very MARCEL DEKKER, INC. • 270 MADISON AVENUE • NEW YORK, NY 10016 ©2003 Marcel Dekker, Inc. All rights reserved. This material may not be used or reproduced in any form without the express written permission of Marcel Dekker, Inc. Cyclohexanone Oxidation 277 high which cause much effect on the production cost of the adipic acid. However the industrial process of oxidation cyclohexane to cyclohexanol and cyclohexanone has become quite efficient. In this paper, we chose Na2WO42H2O as catalyst to oxidize cyclohexanone to adipic acid by 30% hydrogen peroxide in the presence of different acidic ligands. The effects of the kinds of the ligands, the amounts of the ligand and the reaction time on the catalytic reaction are studied. Further researches show that the catalytic system also gives a well catalytic ability for the oxidation of mixture of cyclohexanone and cyclohexanol. Based on these works, we discuss the catalytic mechanism of this kind of catalysis oxidation. EXPERIMENTAL The reagents used in the reaction are analytical purity reagents. 0.825 g Na2WO4H2O (2.5 mmol), desired amounts of acidic ligand and 44.5 mL 30% hydrogen peroxide (440 mmol) were placed in an 100 mL flask, stirred for 10–15 min to get a clear solution at room temperature. Then 10.5 mL cyclohexanone (100 mmol) was added into it without stopping stirring. Continue stirring the reaction mixture at a reflux temperature for 8 h. After reaction was completed the reaction mixture was cooled in the refrigerator for 12 h. Then white crystalline product was obtained after filtration, washed with ice water and dried in the air. The product was weighted and the isolated yield of the adipic acid was calculated which was based on the cyclohexanone that was put in the reaction flask. A melting point tube was used to measure the melting point of the product (the thermometer is not justified). The melting point of the product is mainly between 149 and 151 C (the reported result is 152 C). RESULTS AND DISCUSSION The effect of different acidic ligands on the reaction is showed in Table 1. It can be seen that there is no adipic acid crystalline obtained when no acidic ligand is added into the reaction mixture. The isolated yield increases noticeably when acidic ligand is present. It can be explained that when the ligand is added into catalytic system, it can coordinate with the water soluble sodium tungstate to form a water soluble complex, which is easily to contact with the oil phase, thus the reaction speed is accelerated. The highest yield showed in the Table 1 — 9.45 9.44 10.0 — 4.09 5.10 4.17 1.23 3.22 2.90 2.85 4.21 — — 25 C pKa 0 74.8 72.1 71.1 23.7 62.4 74.3 67.0 58.6 59.7 15.9 70.1 20.4 55.2 44.8 Isolated yield (%) Anthranilic acid Phthalic acid Benzoic acid Hydroxylamine hydrochloride Diaminehydrochloride Hydrazine sulfate Phosphoric acid Phosphorous acid Metaphosphoric acid NaH2PO42H2O NaHSO4 Sulfosalicylic acid Salicylic acid Sulfamic acid p-Toluenesulfonic acid Acidic ligand 2.05 2.95 4.21 — — — 2.12 2.15 — — — — 2.98 — — 25 C pKa The effect of different acidic ligand on the catalytic reaction. 66.3 77.6 1.8 66.7 48.3 61.7 75.0 73.4 3.4 0 73.7 71.2 75.4 66.3 18.1 Isolated yield (%) 278 Reaction conditions: Na2WO42H2O, 2.5 mmol; catalyst/acid ligand ¼ 1/1 (mol ratio); 30% H2O2, 44.5 mL; cyclohexanone, 100 mmol; reaction time, 8 h; reflux temperature. None Pyrocatechol Resorcinol Hydroquinone o-Phenylenediamine 2,4-Dinitrophenol 8-Quinolinol L(þ)Ascorbic acid Oxalic acid Tartaric acid Bromoacetic acid Malonic acid Succinic acid Nicotinic acid i-Nicotinic acid Acidic ligand Table 1. MARCEL DEKKER, INC. • 270 MADISON AVENUE • NEW YORK, NY 10016 ©2003 Marcel Dekker, Inc. All rights reserved. This material may not be used or reproduced in any form without the express written permission of Marcel Dekker, Inc. Zhang et al. MARCEL DEKKER, INC. • 270 MADISON AVENUE • NEW YORK, NY 10016 ©2003 Marcel Dekker, Inc. All rights reserved. This material may not be used or reproduced in any form without the express written permission of Marcel Dekker, Inc. Cyclohexanone Oxidation 279 is 77.6% when phthalic acid is used as the acidic ligand. It also can be seen from Table 1 that for the same kind of ligands, the isolated yield of adipic acid increases with the increasing acidity of the acidic ligand. The acid condition is favored for the oxidation when hydrogen peroxide is used as oxidant, but this is not the only factor. Although the acidity of 8-quinolinol, pyrolatechol, resorcinol and hydroquinone is low, their isolated yield of adipic acid is much higher than that of 2,4-dinitrophenol, and bromoacetic acid. There may be something to do with the coordinate effect of the ligand when it coordinates with sodium tungstate. The pKa value of pyrocatechol, resorcinol and hydroquinone is in the range of 9– 10, however, the isolated yield of adipic acid is very high. Since these phenolic compounds are radical inhibitors, we can infer that the oxidation reaction is not a free radical mechanism but coordination catalysis mechanism. The effect of different amounts of ligands on the reaction is showed in Table 2. Phosophoric acid, sulfosalicylic acid, hydroquinone, Table 2. Acidic ligand Phosphoric acid Sulfosalicylic acid Hydroquinone Pyrocatechol The effect of acidic ligand amount. Ligand amount (mmol) Product isolated yield (%) 1.014 1.523 2.567 5.22 10.22 0.675 1.25 2.5 5.0 10.0 2.5 5.0 10.0 2.5 5.0 10.0 9.6 29.1 75.0 65.7 60.4 27.4 82.1 71.2 71.4 59.6 71.1 76.3 71.1 74.8 78.6 71.7 Reaction condition: Na2WO42H2O, 2.5 mmol; cyclohexanone, 100 mmol; 30% H2O2, 44.5 mL; reaction time, 8 h; reflux temperature. MARCEL DEKKER, INC. • 270 MADISON AVENUE • NEW YORK, NY 10016 ©2003 Marcel Dekker, Inc. All rights reserved. This material may not be used or reproduced in any form without the express written permission of Marcel Dekker, Inc. 280 Zhang et al. pyrocatechol are used with different amounts to study these effects. Table 2 shows that the isolated yield of adipic is low if the amount of acidic ligand is too little and too much. Using sulfosalicylic acid as ligand, the isolated yield of adipic acid reaches the highest when the mole ratio of the catalyst and the ligand is 2/1. When the amount of ligand is too little, sodium tungstate cannot form coordinate complex with ligand thoroughly, which will affect the catalyst to contact with the oil phase. When the ligand is too much, the ligand will form with the Na2WO42H2O to multiple chelate, thus the peroxide bonds in the catalyst structure may be destroyed. This also can be partly proved by the phenomena of using tartaric acid as ligand. Though acid ability of tartaric acid is high, the isolated yield is very low as Table 1 showed because the tartaric acid can coordinate with the catalyst to form multiple chelate. Furthermore, too much ligand dissolved in the reaction mixture will increase the solubility of the product that will decrease the isolated yield, too. Effect of the reaction time on the reaction is showed in Table 3. From Table 3 we can see that the isolated yield of adipic acid increase at first when the reaction time prolonged and reaches the highest isolated yield at 10 and 6.5 h, respectively. Long reaction time leads to the decreasing Table 3. The effect of reaction time on the catalytic oxidation. Acidic ligand Reaction time (h) Product isolated yield (%) Hydroquinone 4 6 8 10 12 14 2 3 4.5 5 6.5 8 70.1 73.5 71.1 76.9 76.4 70.1 9.30 18.8 47.0 59.5 63.7 39.5 L(þ)ascorbic acid Reaction condition: Na2WO42H2O, 2.5 mmol; catalyst/acid ligand ¼ 1/1 (mole ratio); 30% H2O2, 44.5 mL; cyclohexanone, 100 mmol; reflux temperature. MARCEL DEKKER, INC. • 270 MADISON AVENUE • NEW YORK, NY 10016 ©2003 Marcel Dekker, Inc. All rights reserved. This material may not be used or reproduced in any form without the express written permission of Marcel Dekker, Inc. Cyclohexanone Oxidation 281 yield of adipic acid slightly. The further oxidation of the adipic acid to soluble products such as succinic acid and -valeroactone may be the probable reason. Based on the above researches, we investigate the catalytic behavior of catalysis system for the mixture of cyclohexanone and cyclohexanol. The results are summarized in Table 4. The results indicate that the catalysis system exhibit the highest catalytic activity for the oxidation of mixture of cyclohexanol and cyclohexanone with the mole ratio of cyclohexanol and cyclohexanone being 1/2. The isolated yield reaches to 79.1% when sulfosalicylic acid was used as the ligand, but it is still lower than 82.1% isolated yield of adipic acid when pure cyclohexanone is used as substrate. It also shows that the oxidation of cyclohexanol is not easier than that of cyclohexanone. According to the research of Noyori et al., (1998) the oxidation reaction of cyclohexene to obtain adipic acid catalyzed by Na2WO42H2O Table 4. Catalytic oxidation of the mixture of cyclohexanone and cyclohexanol. Ligand Sulfosalicylic acid Hydroquinone Pyrocatechol Ligand amount (mmol) 1 2.5 1.25 2.5 2.5 62.3 68.6 37.5 45.9 Cyclohexanol/cyclohexanone (mol ratio) 4/1 68.6 71.4 44.8 46.2 2/1 72.0 74.8 52.7 50.2 1/1 73.3 76.6 58.3 53.9 1/2 74.3 79.4 61.9 60.3 1/4 73.2 78.2 63.2 52.2 0 71.2 82.1 71.1 74.8 Reaction conditions: Na2WO42H2O, 2.5 mmol; 30%H2O2, 44.5 mL; cyclohexanone þ cyclohexanol ¼ 100 mmol; reaction time, 8 h; reflux temperature. Scheme 1. The proposed reaction mechanism. MARCEL DEKKER, INC. • 270 MADISON AVENUE • NEW YORK, NY 10016 ©2003 Marcel Dekker, Inc. All rights reserved. This material may not be used or reproduced in any form without the express written permission of Marcel Dekker, Inc. 282 Zhang et al. should follow multiple steps involving three kinds of oxidation reactions (olefin epoxidation, two alcohol oxidation, and Baeyer– Villiger oxidation) and hydrolyses. The oxidation of cyclopentanone to obtain -valeroactone by hydrogen peroxide reported by Fischer and Hölderich, (1999) also shows that glutaric acid is one of side product. According to these facts and our research results, the proposed reaction mechanism is depicted in Sch. 1. REFERENCES Bruner, H. S., Lane, S. L., Murphree, B. E. (1998). Manufacture of adipic acid. US Patent 5,710,325. Denis, P., Grosslin, J., Metz, F. (1995). Preparation of adipic acid by hydrocarboxylation of pentenic acids. US Patent 5,420,346. Draths, K. M., Frost, J. W. (1994). Environmentally compatible synthesis of adipic acid from D-glucose. J. Am. Chem. Soc. 116:399. Fischer J., Hölderich, W. F. (1999). Baeyer–Villiger-oxidation of cyclopentanone with aqueous hydrogen peroxide by acid heterogeneous catalysis. Appl. Catal. A: General 180:435. Frost, J. W., Draths, K. M. (1996). Synthesis of adipic acid from biomass-derived carbon sources. US Patent 5,487,987. Gong, H., Jiang, H., Lu, Z. B. (2000). A new green route to the adipic acid. Chem. J. Chinese Universities 21(7):1121. Ma, Z. F., Deng, Y. Q., Wang, K., Cheng, J. (2001). Clean catalytic oxidation to adipic acid. Chemistry Bulletin (Chinese) 2:116. Park, C. M., Goroff, N. S. (1993). One step air oxidation of cyclohexane to produce adipic acid. US Patent 5,221,800. Sato, K., Aoki, M., Noyori, R. (1998). A green route to adipic acid: direct oxidation of cyclohexanes with 30 percent hydrogen peroxide. Science 281:1646. Schulz, J. G. D., Onopchenko, A. (1981). A process for converting cyclohexane to adipic acid. US Patent 4,263,453. Xuan, E. F. (1999). The production and market analysis of adipic acid. Chemical Production and Technology (Chinese) 6(4):59. Received December 31, 2001 Accepted February 23, 2002