Synthesis of acetals and ketals catalyzed by tungstosilicic acid supported on active carbon

Synthesis of acetals and ketals catalyzed by tungstosilicic acid supported on active carbon 1 first-author †E-mail:yangshuijin@163.com †E-mail:yangshuijin@163.com yangshuijin@163.com 1 1 2 Department of Chemistry and Environmental Engineering, Hubei Normal University, Huangshi 435002, China Department of Chemistry and Environmental Engineering, Hubei Normal University, Huangshi 435002, China School of Chemistry and Molecular Sciences, Wuhan University, Wuhan 430072, China School of Chemistry and Molecular Sciences, Wuhan University, Wuhan 430072, China Catalytic activity of activated carbon supported tungstosilicic acid in synthesizing 2-methyl-2-ethoxycarbonylmethyl-1,3-dioxolane, 2,4-dimethyl-2-ethoxycarbonylmethyl-1,3-dioxolane, cyclohexanone ethylene ketal, cyclohexanone 1,2-propa-nediol ketal, butanone ethylene ketal, butanone 1,2-propanediol ketal, 2-phenyl-1,3-dioxolane, 4-methyl-2-phenyl-1,3-dioxolane, 2-propyl-1,3-dioxolane, 4-methyl-2-propyl-1,3-dioxolane was reported. It has been demon-strated that activated carbon supported tungstosilicic acid is an excellent catalyst. Various factors involved in these reactions were investigated. The optimum conditions found were: molar ratio of aldehyde/ketone to glycol is 1/1.5, mass ratio of the catalyst used to the reactants is 1.0%, and reaction time is 1.0 h. Under these conditions, the yield of 2-methyl-2-ethoxycarbonylmethyl-1,3-dioxolane is 61.5%, of 2,4-dimethyl-2-ethoxycarbonylmethyl-1,3-dioxolane is 69.1%, of cyclohexanone ethylene ketal is 74.6%, of cyclohexanone 1,2-propanediol ketal is 80.1%, of butanone ethylene ketal is 69.5%, of butanone 1,2-propanediol ketal is 78.5%, of 2-phenyl-1,3-dioxolane is 56.7%, of 4-methyl-2-phenyl-1,3-dioxolane is 86.2%, of 2-propyl-1,3-dioxolane is 87.5%, of 4-methyl-2-propyl-1,3-dioxolane is 87.9%. Tungstosilicic acid Aceta Ketal Active carbon Catalysis INTRODUCTION 1 Acetals and ketals are among the most important perfume materials and industrial materials of organic synthesis. There are now many methods to synthesize them. The H 2 SO 4 conventionally used as catalyst in factories (Li and Fan, 1981 1981 ) causes many problems, such as erosion of equipment, difficulty for after-treatment, low quality of the products, etc. With the use of anhydrous copper sulfate (Hanzlik and Leinwetter, 1978 1978 ), molecular sieve (Wang and Qian, 1993), montmorillonite K 10 (Li et al., 1996 1996 ), TiSiW 12 O 40 /TiO 2 (Yang et al., 2003a 2003a ), cadmium iodide (Dhrubojyoti et al., 1999 1999 ) as catalysts for the acetals and ketals, the catalytic activity are very high. Catalysts based on heteropolyacids have many advantages over liquid acid catalysts. They are non-corrosive and environmentally friendly, present fewer disposal problems. Their repeated use is possible and their separation from liquid products is easier compared to homogeneous catalysts. Heteropolyacids (HPA) and their salts have been extensively studied because of their interesting catalytic properties (Kozhevnikov, 1998 1998 ; Mizuno and Misono, 1998 1998 ; Yang et al., 2003b 2003b ). Their uses for synthesis of antioxidants, medicinal preparations, vitamins and biologically active substances have been reported and some are already applied in practice. These catalysts are very important for fine chemicals industries, and pharmaceutical and food and flavors industries, etc. HPA and its salts showed excellent catalytic activity accelerating esterification and have recently attracted much attention as catalysts for various industrial processes, because their acidic and redox properties can be controlled at atomic/molecular levels (Wang et al., 1998 1998 ). Kozhevnikov ( 1998 1998 ), Mizuno and Misono ( 1998 1998 ), and Wang et al.( 1998 1998 ) reviewed the homogeneous catalysts and fine organic synthesis products catalyzed by heteropoly compounds. Among heteropolyacids, polytungstic acids are the most widely used catalysts owing to their high acid strength, thermal stability, and low reducibilities. In surface type catalysis, the reactions take place on the internal pore and external surfaces of solid catalysts. In general, the reaction rate is proportional to the catalyst surface area. Supporting the heteropolyacids on solids with high surface areas is a useful method for improving catalytic performance in liquid-solid and gas-solid surface heterogeneous reactions. Activated carbon has been found to be able to entrap a certain amount of heteropoly acids. This work is aimed at studying the interaction between tungstosilicic acid and carbon in catalysts prepared by equilibrium impregnation with water solvent. The species present in all solids were characterized by X-ray powder diffraction and thermogravimetry and differential thermal analysis techniques. Also, the catalyst activity in the acetalation and ketalation reaction was determined. EXPERIMENTAL DETAILS 1 Materials and measurements 2 Ethyl acetoacetate, cyclohexanone, butanone, benzaldehyde, butyraldehyde, glycol, 1,2-propanediol and cyclohexane were of analytical reagent grade. Tungstosilicic acid (H 4 SiW 12 O 40 ) was synthesized as described in literature (Hu et al., 1993 1993 ) and examined by IR spectra. The IR (infrared) spectra were obtained using an IMP 410 IR spectrometer (Nicolet, USA). The X-ray powder diffraction pattern of the powder sample was measured by a D/MAX-3C X-ray diffractometer (Rigaku, Japan) employing CuK α radiation. The data were collected over diffraction angle of 5° to 70° in 2 θ with a step scanning. The accelerating voltage and the applied current were 40 kV and 30 mA, respectively. TG and DTA analysis were carried out with Pyris Diamond TG/DTA thermogravimeter (Perkin-Elmer, USA) in dynamic nitrogen atmosphere and at a heating rate of 10 °C/min. 1 H NMR spectra were determined on a Mercury-VX 300 MHz spectromer with tetramethylsilane as internal standard in CDCl 3 . Preparation of H 4 SiW 12 O 40 /C 2 The solution of tungstosilicic acid was prepared by dissolving 15.0 g tungstosilicic acid in 40 ml of water solution. The support used was commercial wood-based activated carbon (C) ground to mean particle size of 1 mm, with a surface area of 950 m 2 /g and average pore diameter below 2 nm. Before being utilized, this material was washed first in solution of NaOH 0.1 mol/L, then in HCl 0.1 mol/L to eliminate the soluble acidic and alkaline impurities. Finally, it was chemically treated in solution of HNO 3 (30%, w/v) and heated by reflux for 2 h. The treatment with nitric acid makes the carbon more acidic. Then 5.0 g activated carbon was dropped into the above solution under vigorous stirring, and the resulting solution was impregnated for 6 h. Black solid H 4 SiW 12 O 40 /C washed with distilled water, the powder was dried under 105 °C for 24 h. Finally the catalysts were stored in a desiccator till time of use. H 4 SiW 12 O 40 /C were identified by XRD and TG/DTA. Synthesis of acetals and ketals 2 The reaction was carried out in a three-neck flask (100 ml) equipped with a stirrer, a reflux condenser and a thermometer. The molar ratio of glycol to aldehyde/ketone was 1.5:1, 0.2 mol ethyl acetoacetate, cyclohexanone, butanone, benzaldehyde, butyraldehyde were added separately with 0.3 mol glycol (ethylene glycol or 1,2-propylene glycol) to the catalyst. The solution was heated to boiling and refluxed until no water flowed off. Then the solution was distilled to get colourless liquid as the end product. RESULTS AND DISCUSSION 1 Characterization of catalyst H 4 SiW 12 O 40 /C 2 1. XRD spectra 3 The X-ray diffraction pattern of H 4 SiW 12 O 40 /C is shown in Fig. 1 1 . X-ray powder diffraction analysis is used widely to study the structure of heteropoly complexes. The wide diffusive peak at 27° for C in the X-ray diffraction pattern verifies its amorphous nature. 2. Thermal behavior studies 3 The TG-DTA patterns of H 4 SiW 12 O 40 /C are shown in Fig. 2 2 . In the DTA diagram of H 4 SiW 12 O 40 /C, the exothermic peak was assigned to the Keggin’s anion decomposition at 579 °C. The TG diagram of the sample shows a decrease of the weight below 444.3 °C (less than 2.1%) and a rapid and continuous weight loss from 444.3 °C to 693.9 °C (almost 74.6%). Thermal behavior of H 4 SiW 12 O 40 /C is similar to that of H 4 SiW 12 O 40 . In the H 4 SiW 12 O 40 sample, it was observed the endothermic peak associated with appearance of the anhydrous phase H 4 SiW 12 O 40 is seen at 169 °C, and the exothermin peak assigned to the Keggin’s anion decomposition at 526 °C. Evolutionary operation experiment design of reaction conditions 2 For example, butyraldehyde glycol acetal was synthesized from butyraldehyde and glycol in the presence of H 4 SiW 12 O 40 /C. The factors influencing the synthesis were discussed and the best conditions were found. 1. Effect of molar ratio of butyraldehyde to glycol on yield 3 Table 1 1 shows the effect of molar ratio of butyraldehyde to glycol on yield. The molar ratio of butyraldehyde to glycol directly influences the yield. Butyraldehyde: 0.2 mol; mass ratio of catalyst to reactants: 1.0%; temperature: 86~113 °C; reaction time: 60 min n (butyraldehyde): n (glycol) 1:1.3 1:1.4 1:1.5 1:1.6 1:1.7 Yield (%) 84.1 84.9 87.5 86.2 86.2 The yield increases with the increase of molar ratio of butyraldehyde to glycol. When the ratio is 1:1.5, the yield is the highest. To increase molar ratio of butyraldehyde to glycol will cause a lower yield, because of the lowering of the temperature. So the optimum molar ratio of butyraldehyde to glycol is 1:1.5. 2. Effect of catalyst dosage on the yield 3 The effect of catalyst dosage on the yield is shown in Table 2 2 . Butyraldehyde: 0.2 mol; mole ratio of butyraldehyde to glycol: 1:1.5; temperature: 86~113 °C; reaction time: 60 min Catalyst dosage (%) 0.5 0.75 1.0 1.25 Yield (%) 80.1 80.6 87.5 86.2 Table 2 2 shows that the yield increases with increase of the catalyst concentration. When the mass ratio of the catalyst to the reactants was 1.0%, the yield was 87.5 %. The yield did not vary greatly when more catalyst was added. Therefore, the mass ratio of the catalyst to the reactants was 1.0 % for these experiments. 3. Effect of reaction time on the yield 3 Reaction time is also an important factor for the reaction. Table 3 3 shows the effect of the reaction time on the yield. Butyraldehyde: 0.2 mol; mole ratio of butyraldehyde to glycol: 1:1.5; mass ratio of catalyst to reactants: 1.0%; temperature: 86~113 °C Reaction time (min) 40 60 80 100 Yield (%) 83.2 87.5 82.3 77.6 We can see from Table 3 3 that the yield increases with increase of time. After 60 min, the yield is the highest. So we choose 60 min as optimum reaction time. Comparison of catalytic activity of different catalysts 2 Table 4 4 gives the catalytic activity of FeCl 3 ·6H 2 O (Yu and Peng, 1994 1994 ), TiO 2 /SO 4 2− (Wang et al., 1992a 1992a ), Fe 2 (SO 4 ) 3 · x H 2 O (Li et al., 1989 1989 ), and H 4 SiW 12 O 40 /C. Butyraldehyde: 0.2 mol; mole ratio of butyraldehyde to glycol: 1:1.5; mass ratio of catalyst to reactants: 1.0%; temperature: 86~113 °C Catalyst n (butyraldehyde): n (glycol) Reaction time (h) Yield (%) FeCl 3 ·6H 2 O 1:1.5 1.5 73.9 TiO 2 /SO 4 2− 1:1.5 1.5 67.0 Fe 2 (SO 4 ) 3 · x H 2 O 1:1.5 6.0 56.0 H 4 SiW 12 O 40 /C 1:1.5 1.0 87.5 The following conclusions were obtained: All of the catalysts showed certain catalytic activity for the synthesis of 2-propyl-1,3-dioxolane, with the catalytic activity of H 4 SiW 12 O 40 /C being the highest among these four catalysts. Analysis and identification of the product 2 A purified product was analyzed by IR and 1 H NMR spectrum. The IR spectrum of 2-propyl-1,3-dioxolane shows peaks at 1146, 1123, 1057, 1023, 946 cm −1 , which are in accordance with the standard IR spectrum of 2-propyl-1,3-dioxolane; 1 H NMR (CDCl 3 , 300 Hz): 4.60 (m, 1H, CH), 3.83 (m, 4H, OCH 2 CH 2 O), 1.63 (m, 2H, CH 2 ), 1.25 (m, 2H, CH 2 ), 0.96 (t, 3H, CH 3 ); n D 20 =1.4190 ( n D 20 =1.4182 (Wang et al., 1992a 1992a )); b.p.: 130~133 °C. SYNTHESIS OF ACETALS AND KETALS 1 Factors on the synthesis of acetals and ketals 2 Syntheses of ten important acetals and ketals were carried out as follows. The amount of reactant of aldehyde/ketone was fixed to 0.2 mol with cyclohexane (8 ml) as water-stripped reagent. The results of these synthesis reactions are summarized in Fig. 3 3 and Table 5 5 . Reaction conditions: mole ratio of aldehyde/ketone to glycol: 1:1.5; mass ratio of catalyst to reactants: 1.0%; reaction time: 1.0 h Product b.p. (°C) n D 20 Yield (%) IR (cm −1 ) 1 H-NMR ( δ ) 1a 126–128/6.7 kPa 1.4321 61.5 1738, 1375, 1244, 1188, 1047 4.16, 3.98, 2.62, 1.46, 1.22 1b 150–155/6.7 kPa 1.4278 69.1 1740, 1377, 1244, 1188, 1043 4.10, 3.98, 3.42, 2.53, 1.30, 1.20 2a 176–180 1.4580 74.6 2937, 2863, 1163, 1104 3.91, 1.58 2b 172–176 1.4493 80.1 2937, 2864, 1163, 1103 4.12, 3.95, 3.34, 2.28, 1.19, 1.21 3a 116–119 1.4106 69.5 1254, 1215, 1194, 1130 3.90, 1.62, 1.31, 0.94 3b 126–129 1.4101 78.5 1250, 1218, 1194, 1157 4.11, 3.83, 3.34, 1.60, 1.34, 1.26, 0.90 4a 224–228 1.5264 56.7 1096, 1071, 1028, 947 7.37, 5.82, 4.05, 3.70 4b 218–222 1.5095 86.2 1097, 1067, 1011, 976 7.40, 5.97, 5.81, 4.10, 3.50, 1.38, 1.32 5a 130–133 1.4190 87.5 1146, 1123, 1023, 946 4.60, 3.83, 1.63, 1.25, 0.96 5b 140–144 1.4152 87.9 1150, 1123, 1024, 970 4.87, 4.10, 3.93, 3.35, 1.58, 1.40, 1.25, 0.96 From the data listed in Table 5 5 , we can find that H 4 SiW 12 O 40 /C was highly active, leading to yields of ten ketals and acetals up to 87.9% and no less than 56.7% after 1.0 h. Moreover, the reaction temperature was controlled at the reflux temperature and the amount of H 4 SiW 12 O 40 /C was much lower than other catalyst used in these reactions (Wang et al., 1992b 1992b ; Zhang et al., 1995 1995 ). All these helped to solve the technical problems faced by the industrial processes. Characterization of acetals and ketals 2 The products have been purified and confirmed by the measurement of infrared spectrum and 1 H NMR. IR and 1 H NMR spectral data on acetals or ketals (1a~5b) are listed in Table 5 5 . CONCLUSION 1 The optimum conditions of synthesis for 2-propyl-1,3-dioxolane are: molar ratio of butyraldehyde to glycol is 1:1.5, and catalyst dosage used is 1.0% of feed stocks, and the reaction time is 60 min. Under the above conditions, the yield of 2-propyl-1,3-dioxolane can be up to 87.5%. Activated carbon supported tungstosilicic acid was applied as catalyst in the synthesis of ten important ketals and acetals and revealed high catalytic activity. Under certain conditions (molar ratio of aldehyde/ketone to glycol is 1:1.5, the mass ratio of the catalyst used in the reactants is 1.0%, the reaction time is 1.0 h), the yields of ketals and acetals can reach 56.7%~87.9%. It has been demonstrated that the activated carbon supported tungstosilicic acid is an excellent catalyst. From the above results and discussion, we can see that the synthesis of ten important ketals and acetals by the activated carbon supported tungstosilicic acid has good prospects. References DL Dhrubojyoti , P Dipak , SS Jagir . Cadmium iodide catalyzed and efficient synthesis of acetals under microwave irradiations . Chemistry Letters , 1999 . 332 ( 8 ): 1283 - 1284 . . Cadmium iodide catalyzed and efficient synthesis of acetals under microwave irradiations RP Hanzlik , M Leinwetter . Reactions of epoxides and carbonyl compounds catalyzed by anhydrous copper sulfate . J Org Chem , 1978 . 43 ( 3 ): 438 - 440 . . 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Catalytic synthesis of acetals and ketals with heteropolyacid 10.1631/jzus.2005.B0373 Project supported by the Natural Science Foundation of Hubei Province Education Committee (No. 2004D007) and the National Natural Science Foundation of China (No. 20471044) 2004-10-24 2005-01-08 2005-04-10 2022-01-05 Copyright © 2005, Journal of Zhejiang University Science 2005 Journal of Zhejiang University-SCIENCE B (Biomedicine and Biotechnology) 05 6B