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International Journal of Chemical Engineering
Volume 2014 (2014), Article ID 481627, 7 pages
Catalytic Cascade Dehydration-Etherification of Fructose into 5-Ethoxymethylfurfural with SO3H-Functionalized Polymers
State-Local Joint Laboratory for Comprehensive Utilization of Biomass, State Key Laboratory Breeding Base of Green Pesticide and Agricultural Bioengineering (Ministry of Education), Center for Research and Development of Fine Chemicals, Guizhou University, Guiyang 550025, China
Received 24 October 2013; Revised 14 March 2014; Accepted 15 March 2014; Published 31 March 2014
Academic Editor: Donald L. Feke
Copyright © 2014 Hu Li et al. This is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.
A series of SO3H-functionalized polymers were prepared and employed as heterogeneous catalysts for one-pot transformation of fructose into 5-ethoxymethylfurfural (EMF) that is considered to be one of potential liquid biofuels. A high EMF yield of 72.8% could be obtained at 110°C for 10 h, and the polymeric acid catalysts could be recycled for five times without significant loss of catalytic performance.
With the increasing concerns about the depletion of fossil resources, environmental pollution, and global warming, biomass which is abundant, widespread, and an ideal substitute for unsustainable resources has attracted worldwide attention . Much effort has been made to develop processes for the efficient conversion of biomass resources into biofuels and value-added chemicals [2–6]. Amongst the existing alternatives, 5-hydroxymethylfurfural (HMF), furfural and other furanic derived products have received wide attention and showed great potential in the replacement of fuels and chemicals currently produced from fossil resources . In particular, 5-ethoxymethylfurfural (EMF) has high energy density of 8.7 kWh/L, which is thereby proposed to be one of potential liquid biofuels .
In the presence of metal chlorides, mineral acids, or solid acids, EMF could be synthesized from 5-chloromethylfurfural (CMF), HMF, and carbohydrates such as fructose (Scheme 1). As one of the initiators, Mascal and Nikitin  reported that CMF might emerge as a central intermediate in the conversion of carbohydrate-based material into EMF. Starting from HMF, Che et al.  illustrated that H4SiW12O40/MCM-41 nanospheres were efficient for production of EMF with selectivity of 84.1% at HMF conversion of 92.0%. In contrast to Brønsted acids facilitating for the formation of ethyl-4-oxopentanoate, solid catalysts with strong Lewis acid sites (e.g., introduction of ZrO2 into SBA-15 or presence of extraframework isolated Al3+ sites in MCM-41) could afford a higher yield to EMF (up to 76%) with HMF conversion of 100% at 140°C for 5 h . With respect to one-pot catalytic conversion of carbohydrates into EMF, reaction systems containing AlCl3, FeCl3, NH4Cl, or H3PW12O40 were capable of successively catalyzing dehydration of fructose to HMF and etherification of HMF with ethanol to EMF [12–18]. From an economical and environmental point of view, heterogeneous catalysts were further developed for the sequential dehydration-etherification of carbohydrates into EMF. Silica coated magnetic Fe3O4 nanoparticles and K-10 clay supported phosphotungstic acid were demonstrated to be efficient for the synthesis of EMF from fructose, giving a maximum EMF yield of 54.8% and 61.5%, respectively [19, 20]. Two different types of solid acid catalysts (i.e., Brønsted acid Amberlyst 131 and Lewis acid zeolite Sn-BEA) were simultaneously employed for conversion of glucose to EMF, and a moderate yield of EMF (31%) could be achieved in ethanol in a single reactor at 90°C .
Besides, sulfonic acid functionalized catalysts were illustrated to exhibit highly efficient catalytic performance for selective conversion of fructose into EMF. Kraus and Guney  found SO3H-functionalized ionic liquids used together with hexane resulting in a 54% isolated yield from fructose at 100°C for 80 min. Using silica supported sulfonic acid as a heterogeneous catalyst, EMF could be obtained in a high yield of 63.1% from fructose at 100°C for 24 h . A cellulose sulfuric acid was also synthesized and used as an efficient and environmentally friendly biosupported catalyst for the synthesis of EMF from fructose, giving a high EMF yield of 72.5% through one-pot reaction at 100°C within 12 h . It should be noted that a much higher EMF yield of 90.5% could be obtained from fructose with the presence of methylimidazolebutylsulfate phosphotungstate ([MIMBS]3PW12O40) at 90°C for 24 h . In the present study, a series of SO3H-functionalized polymers were hereby prepared and further employed for the catalytic conversion of fructose into EMF in one-pot.
2. Experimental Part
Azobisisobutyronitrile (AIBN), 1-vinylimidazole, 1,3-propanesultone, H3PW12O40 (PW), fructose, EMF (98%), and HMF (98%) were purchased from Shanghai Aladdin Industrial Inc.; acetone, methanol, ethanol (99.5%), HCl, H2SO4, and CF3COOH were purchased from Chongqing Chuandong Chemical Reagent Company. All chemicals were of analytical grade and used as received, unless otherwise noted.
2.2. Preparation of Poly(VMPS)-PW and Poly(VMPS)-Cl
Firstly, poly(VMPS) was synthesized as reported in the previous literature . Then, an aqueous solution of H3PW12O40 (4 g, 1.39 mmol) or HCl (4.17 mmol) was added to the solution of Poly(VMPS) (0.88 g, monomer molar quantity was 4.17 mmol) dispersed in methanol, followed by stirring of the mixture at 60°C for 24 h. On completion, water and methanol were removed in vacuum to afford the final product poly(VMPS)-PW (or poly(VMPS)-Cl) as a solid .
For comparison, three other solid acidic ionic liquid polymers DVB-[C3vim][CO2CF3], DVB-[C3vim][Cl], and DVB-[C3vim][HSO4] were also prepared from divinylbenzene (DVB) and corresponding Brønsted acidic ionic liquids [SO3H (CH2)3vim][X] (X = CO2CF3, Cl, and HSO4) respectively, according to the reported procedures [28, 29]. As illustrated in Figure 1, all the prepared solid catalysts consist of SO3H functionalized ionic liquids and corresponding polymers.
2.3. Catalyst Characterization
XRD patterns were recorded with Rigaku D/Max-2200 X-ray powder diffractometer using Ni-filtered Cu Kα radiation source. FT-IR spectra were measured on a Nicolet 360 FT-IR instrument (KBr discs). TG analysis was performed with a Netzsch STA449C Jupiter instrument in dry air at a heating rate of 10°C/min. NH3-TPD was carried out on an AutoChem 2920 chemisorption analyzer.
2.4. Typical Procedure for Catalytic Transformation of Fructose into EMF
The synthesis of EMF from fructose was performed in a sealed tube (Ace, pressure limit: 20 bar) under magnetic stirring. In a typical procedure, to a stock solution of fructose (50 mg) dissolved in ethanol (2 mL), a SO3H functionalized polymer (10 mg) was introduced. The resulting mixture was stirred magnetically and heated with an oil bath at a certain temperature for a specific time. After the reaction and separation of the catalyst, the obtained solution was decanted into a volumetric flask using ethanol as diluents and analyzed by high performance liquid chromatography.
2.5. Analysis Methods
HMF and EMF were analyzed by high-performance liquid chromatography (HPLC; Agilent 1100, USA) fitted with a Lichrospher C18 column and an ultraviolet (UV) detector at 280 nm. The column oven temperature was set at 30°C, and the mobile phase was 0.1 wt% acetic acid/acetonitrile (85/15, v/v) at a flow rate of 1.0 mL/min.
The concentration of HMF and EMF was calculated based on the standard curve obtained with the standard substances. HMF yield (X, mol%) and EMF yield (Y, mol%) were calculated as follows: X(%) = (mole concentration of HMF)/(mole concentration of initial fructose) × 100% Y(%) = (mole concentration of EMF)/(mole concentration of initial fructose) × 100%.
2.6. Recycling of Catalysts
The catalyst was recovered by centrifugation, washing with acetone for three times, and drying at 60°C for 2 h. The recovered catalyst was directly used for the next run.
3. Results and Discussion
3.1. Catalyst Characterization
FTIR spectra and XRD patterns on the prepared –SO3H functionalized polymers were performed (Figures 2(a) and 2(b)). In Figure 2(a), two significant bands at 1166 cm−1 and 1040 cm−1 are attributable to the asymmetric and symmetric stretching vibrations of S=O, respectively. As to poly(VMPS)-PW, 1080 cm−1 (P–Oa), 975 cm−1 (W=Od), 898 cm−1 (W–Ob–W) (corner-sharing), and 810 cm−1 (W–Oc–W) (edge-sharing) are assigned to a Keggin structure of . Although, the XRD pattern of H3PW12O40 displays a series of featured diffraction peaks (Figure 2(b)), XRD patterns for poly(VMPS)-PW as well as poly(VMPS)-Cl only show broad diffraction peaks, indicating the loss of the long-range crystal order for the polymeric ionic hybrid and the rearrangement of the Keggin anions during the self-assembly of polymeric cations with heteropolyanions .
Figure 2 also demonstrates the TG analysis of poly(VMPS)-PW and poly(VMPS)-Cl. In both samples, the decomposition temperatures are above 300°C (Figure 2(c)). As the temperature increases to over 350°C, the PW-based catalyst sample (poly(VMPS)-PW) exhibits much better thermal stability compared with Cl-based sample (poly(VMPS)-Cl).
To determine the distribution of acid strength and the relative acid amount for the catalysts, the NH3-TPD was carried out and the profiles were revealed in Figure 3. The peak maximums of all the catalyst samples appear at the temperature ranging from 300 to 500°C, implying that the acidic centers of the sample are related to medium strong acid sites of –SO3H groups. It is worth noting that even though all the catalysts are functionalized with ionic liquids bearing SO3H groups, the acid strength as well acid density is greatly influenced by both polymers and anions (Table 1). Obviously, DVB-[C3vim][HSO4] catalyst was found to exhibit the highest acid density with different acid strengths.
3.2. Catalytic One-Pot Dehydrative Etherification of Fructose into EMF with Various –SO3H Functionalized Polymeric Catalysts
Initially, various –SO3H functionalized polymeric catalysts were prepared and further employed to evaluate their catalytic performance for one-pot dehydrative etherification of fructose into EMF, and the results are summarized in Figure 4. –SO3H functionalized DVB polymers were demonstrated by NH3-TPD to possess relatively higher acid density as compared with poly(VMPS)-PW and poly(VMPS)-Cl, which were well illustrated by the corresponding relatively higher fructose conversions (>95%). Nevertheless, DVB polymers supported sulfonate catalysts only exhibited moderate reactivity in terms of EMF yields (up to ~36%) and low HMF yields (around 4%) directly generated from fructose. In contrast, a high EMF yield of 48.9% together with 5.3% HMF yield was obtained when using a solid-liquid biphasic system consisting of the catalyst poly(VMPS)-PW and ethanol. While poly(VMPS)-Cl exhibited relatively lower catalytic activity, which might be attributed to the poor mass transfer of the catalyst since it was attached onto the bottom surface of the flask reactor at high reaction temperature. Besides HMF and EMF as well as humins formed during the process of catalytic conversion of fructose with SO3H-functionalized polymers, a certain amount of ethyl levulinate and 5-ethoxymethylfurfural diethyl acetal were also detected by HPLC .
3.3. Effect of Reaction Temperature and Time on One-Pot Dehydrative Etherification of Fructose into EMF
Since poly(VMPS)-PW was investigated to exhibit the best catalytic performance of all the screened catalysts, the effect of reaction temperature and time on the synthesis of EMF from fructose was further carried out with the same catalyst. Reactions were conducted at reaction temperature of 90, 110, and 130°C within reaction time of 1, 4, 7, 10, and 15 h, respectively, and the results are shown in Figure 5. It was demonstrated that EMF yields were gradually increased to 60.7% and 71.3% with the increase of reaction time from 1 to 15 h at reaction temperature of 90 and 110°C, respectively. Nevertheless, at the higher temperature of 130°C, the maximum EMF yield could be obtained in 60.1% for 4 h, which was then slowly decreased to 31.2% for 15 h. It was noted that the yield of HMF only increased with the relatively lower reaction temperature of 90°C at the early reaction stage and the increasing rate for EMF yield was slowed down or even reduced after a long reaction period, indicating that much more side products were formed at high temperature of 130°C or after a long reaction time. Taking above discussions into consideration, reaction temperature of 110°C and reaction time of 10 h were selected as the optimized reaction conditions and employed for the following studies.
3.4. Effect of Catalyst Loading on One-Pot Dehydrative Etherification of Fructose into EMF
The effect of catalyst loading on direct dehydrative etherification of fructose into EMF was also investigated, and the results are illustrated in Figure 6. It was clearly shown that increasing the catalyst dosage of poly(VMPS)-PW from 5 mg to 20 mg correspondingly resulted in a significant increase in EMF yield from 59.3% to 72.8% at 110°C for 10 h, which should be ascribed to the increased availability and number of active sites. Simultaneously, the tendency in HMF yield with the increase of catalyst dosage implied the gradually enhanced conversion of fructose and HMF. From an economical and environmental point of view, 20 mg might be an appropriate catalyst loading for the one-pot dehydrative etherification of fructose into EMF with high yield.
3.5. Reusability of Poly(VMPS)-PW for One-Pot Conversion of Fructose into EMF
Catalyst recycling is one of essential aspects for practical applications. The study on reusability of poly(VMPS)-PW for one-pot conversion of fructose into EMF was carried out at 110°C for 10 h. After the reaction of each run, the catalyst was recovered by centrifugation, washing with acetone for three times and drying at 60°C for 2 h. The recovered catalyst was directly used for the next run, and these steps were repeated five times. As shown in Figure 7, the EMF yields were remained around 60% within every cycle. These results indicated that the –SO3H functionalized polymeric catalyst could be effectively separated and reused for the one-pot cascade dehydration-etherification reaction.
In summary, the SO3H-functionalized polymeric catalyst was efficient for direct conversion of fructose into EMF, and a maximum EMF yield of 72.8% was achieved at 110°C within 10 h. Moreover, the heterogeneous catalyst could be reused several times with no significant reduction in catalytic reactivity.
Conflict of Interests
The authors declare that there is no conflict of interests regarding the publication of this paper.
This work was financially supported by the International Science & Technology Cooperation Program of China (2010DFB60840), Social Development S&T Program (no. SZ- 3011), National Key Technology R&D Program (2006BAD07A12), and State Scholarship Fund (no. 201306670004).
- L. Hu, G. Zhao, W. Hao et al., “Catalytic conversion of biomass-derived carbohydrates into fuels and chemicals via furanic aldehydes,” RSC Advances, vol. 2, pp. 11184–11206, 2012.
- P. L. Dhepe and A. Fukuoka, “Cellulose conversion under heterogeneous catalysis,” ChemSusChem, vol. 1, no. 12, pp. 969–975, 2008.
- D. M. Alonso, S. G. Wettstein, and J. A. Dumesic, “Bimetallic catalysts for upgrading of biomass to fuels and chemicals,” Chemical Society Reviews, vol. 41, pp. 8075–8098, 2012.
- J. A. Geboers, S. van de Vyver, R. Ooms, B. Op De Beeck, P. A. Jacobs, and B. F. Sels, “Chemocatalytic conversion of cellulose: opportunities, advances and pitfalls,” Catalysis Science and Technology, vol. 1, no. 5, pp. 714–726, 2011.
- J. J. Verendel, T. L. Church, and P. G. Andersson, “Catalytic one-pot production of small organics from polysaccharides,” Synthesis, no. 11, pp. 1649–1677, 2011.
- Y. C. Lin and G. W. Huber, “The critical role of heterogeneous catalysis in lignocellulosic biomass conversion,” Energy and Environmental Science, vol. 2, no. 1, pp. 68–80, 2009.
- H. Li, Q. Zhang, P. S. Bhadury, and S. Yang, “Furan-type compounds from carbohydrates via heterogeneous catalysis,” Current Organic Chemistry, 2014.
- E. J. Ras, S. Maisuls, P. Haesakkers, G. J. Gruter, and G. Rothenberg, “Selective hydrogenation of 5-ethoxymethylfurfural over alumina-supported heterogeneous catalysts,” Advanced Synthesis & Catalysis, vol. 351, pp. 3175–3185, 2009.
- M. Mascal and E. B. Nikitin, “Direct, high-yield conversion of cellulose into biofuel,” Angewandte Chemie—International Edition, vol. 47, no. 41, pp. 7924–7926, 2008.
- P. Che, F. Lu, J. Zhang et al., “Catalytic selective etherification of hydroxyl groups in 5-hydroxymethylfurfural over H4SiW12O40/MCM-41 nanospheres for liquid fuel production,” Bioresource Technology, vol. 119, pp. 433–436, 2012.
- P. Lanzafame, D. M. Temi, S. Perathoner et al., “Etherification of 5-hydroxymethyl-2-furfural (HMF) with ethanol to biodiesel components using mesoporous solid acidic catalysts,” Catalysis Today, vol. 175, no. 1, pp. 435–441, 2011.
- Y. Yang, C. Hu, and M. M. Abu-Omar, “Conversion of glucose into furans in the presence of AlCl3 in an ethanol-water solvent system,” Bioresource Technology, vol. 116, pp. 190–194, 2012.
- B. Liu, Z. Zhang, K. Huang, and Z. Fang, “Efficient conversion of carbohydrates into 5-ethoxymethylfurfural in ethanol catalyzed by AlCl3,” Fuel, vol. 113, pp. 625–631, 2013.
- X. Jia, J. Ma, P. Che et al., “Direct conversion of fructose-based carbohydrates to 5-ethoxymethylfurfural catalyzed by AlCl3·6H2O/BF3·(Et)2O in ethanol,” Journal of Energy Chemistry, vol. 22, pp. 93–97, 2013.
- X. Zhou, Z. Zhang, B. Liu, Q. Zhou, S. Wang, and K. Deng, “Catalytic conversion of fructose into furans using FeCl3 as catalyst,” Journal of Industrial and Engineering Chemistry, vol. 20, no. 2, pp. 644–649, 2013.
- J. Liu, Y. Tang, K. Wu, C. Bi, and Q. Cui, “Conversion of fructose into 5-hydroxymethylfurfural (HMF) and its derivatives promoted by inorganic salt in alcohol,” Carbohydrate Research, vol. 350, pp. 20–24, 2012.
- Y. Yang, M. M. Abu-Omar, and C. Hu, “Heteropolyacid catalyzed conversion of fructose, sucrose, and inulin to 5-ethoxymethylfurfural, a liquid biofuel candidate,” Applied Energy, vol. 99, pp. 80–84, 2012.
- H. Wang, T. Deng, Y. Wang, Y. Qi, X. Hou, and Y. Zhu, “Efficient catalytic system for the conversion of fructose into 5-ethoxymethylfurfural,” Bioresource Technology, vol. 136, pp. 394–400, 2013.
- S. Wang, Z. Zhang, B. Liu, and J. Li, “Silica coated magnetic Fe3O4 nanoparticles supported phosphotungstic acid: a novel environmentally friendly catalyst for the synthesis of 5-ethoxymethylfurfural from 5-hydroxymethylfurfural and fructose,” Catalysis Science & Technology, vol. 3, pp. 2104–2112, 2013.
- A. Liu, B. Liu, Y. Wang, R. Ren, and Z. Zhang, “Efficient one-pot synthesis of 5-ethoxymethylfurfural from fructose catalyzed by heteropolyacid supported on K-10 clay,” Fuel, vol. 117, pp. 68–73, 2014.
- C. M. Lew, N. Rajabbeigi, and M. Tsapatsis, “One-pot synthesis of 5-(Ethoxymethyl)furfural from glucose using Sn-BEA and Amberlyst catalysts,” Industrial and Engineering Chemistry Research, vol. 51, no. 14, pp. 5364–5366, 2012.
- G. A. Kraus and T. Guney, “A direct synthesis of 5-alkoxymethylfurfural ethers from fructose via sulfonic acid-functionalized ionic liquids,” Green Chemistry, vol. 14, pp. 1593–1596, 2012.
- B. Liu and Z. Zhang, “One-pot conversion of carbohydrates into 5-ethoxymethylfurfural and ethyl D-glucopyranoside in ethanol catalyzed by a silica supported sulfonic acid catalyst,” RSC Advances, vol. 3, pp. 12313–12319, 2013.
- B. Liu, Z. Zhang, and K. Huang, “Cellulose sulfuric acid as a bio-supported and recyclable solid acid catalyst for the synthesis of 5-hydroxymethylfurfural and 5-ethoxymethylfurfural from fructose,” Cellulose, vol. 20, pp. 2081–2089, 2013.
- L. Bing, Z. Zhang, and K. Deng, “Efficient one-pot synthesis of 5-(ethoxymethyl)furfural from fructose catalyzed by a novel solid catalyst,” Industrial & Engineering Chemistry Research, vol. 51, pp. 15331–15336, 2012.
- Y. Leng, P. Jiang, and J. Wang, “A novel Brønsted acidic heteropolyanion-based polymeric hybrid catalyst for esterification,” Catalysis Communications, vol. 25, pp. 41–44, 2012.
- H. Li, Q. Zhang, X. Liu et al., “Immobilizing Cr3+ with SO3H-functionalized solid polymeric ionic liquids as efficient and reusable catalysts for selective transformation of carbohydrates into 5-hydroxymethylfurfural,” Bioresource Technology, vol. 144, pp. 21–27, 2013.
- G. Fan, C. Liao, T. Fang, M. Wang, and G. Song, “Hydrolysis of cellulose catalyzed by sulfonated poly(styrene-co-divinylbenzene) in the ionic liquid 1-n-butyl-3-methylimidazolium bromide,” Fuel Processing Technology, vol. 116, pp. 142–148, 2013.
- F. Liu, L. Wang, Q. Sun, L. Zhu, X. Meng, and F. S. Xiao, “Transesterification catalyzed by ionic liquids on superhydrophobic mesoporous polymers: heterogeneous catalysts that are faster than homogeneous catalysts,” Journal of the American Chemical Society, vol. 134, pp. 16948–16950, 2012.
- H. Li, X. He, Q. Zhang et al., “Polymeric ionic hybrid as solid acid catalyst for the selective conversion of fructose and glucose to 5-hydroxymethylfurfural,” Energy Technology, vol. 1, pp. 151–156, 2013.
- M. M. Antunes, P. A. Russo, P. V. Wiper et al., “Sulfonated graphene oxide as effective catalyst for conversion of 5-(hydroxymethyl)-2-furfural into biofuels,” ChemSusChem, vol. 7, pp. 804–812, 2014.