Simple efficient one-pot synthesis of 5-hydroxymethylfurfural and 2,5-diformylfuran from carbohydrates

Quentin Girka ab, Boris Estrine *b, Norbert Hoffmann *a, Jean Le Bras a, Siniša Marinković b and Jacques Muzart a
aCNRS, Université de Reims Champagne-Ardenne, Institut de Chimie Moléculaire de Reims, UMR 7312, UFR des Sciences Exactes et Naturelles, 51687 Reims, France. E-mail: norbert.hoffmann@univ-reims.fr
bAgro-Industrie Recherches et Développements, Green Chemistry Departement, Route de Bazancourt, 51110 Pomacle, France. E-mail: b.estrine@a-r-d.fr

Received 21st July 2015 , Accepted 1st September 2015

First published on 4th November 2015


Abstract

2,5-Diformylfuran (DFF) and 5-hydroxymethylfurfural (HMF) are interesting platform compounds in the chemical industry. A sustainable one-pot procedure is reported for the transformation of carbohydrates into DFF. Mono-, di- and polysaccharides as well as crude biomass (straw and bran) have been transformed. Depolymerisation, glucose isomerisation to fructose, fructose dehydration and finally oxidation of HMF to DFF are involved. The optimised catalytic system contains boric acid in DMSO for HMF synthesis. Addition of sodium bromide and formic acid to the reaction mixture leads to the formation of DFF. Boric acid is mainly involved in depolymerization, isomerisation and dehydration. Large amounts of boric acid lead to the degradation of HMF. NaBr and water are involved in the selective oxidation of HMF. Formic acid is involved in the dehydration step and it accelerates the oxidation of HMF.


Introduction

Fossil resources are the main source of carbon-based compounds in chemical and energy industries. Taking into account fossil carbon reserve depletion, biomass appeared as the most reliable source for carbon-containing substances.1–3 The production of biomass by nature is estimated to be about 2 × 1011 tons per year.4 About 75% of these materials are carbohydrates which are essentially produced by green plants using photosynthesis to transform carbon dioxide back into biomass. In this context, biomass is considered as the basis for renewable fuels and chemicals. However, processes in the chemical industry are most often optimised for the transformation of compounds obtained from fossil resources, mainly mineral oil. While this material is characterised by low oxygen content, carbohydrate-based biomass generally has high oxygen content. One strategy for using biomass in the chemical industry is to develop new processes for new products with interesting properties. Another or a complementary strategy is to develop processes for the transformation of biomass into platform chemicals or intermediates which can be further transformed using established technologies in the chemical industry. In this context, dehydration of carbohydrates is an interesting transformation since furan derivatives are obtained. These compounds are versatile key intermediates not only for industrial chemistry but also for organic synthesis in general. While dehydration of pentose-containing biomass leading to furfural is more or less easy,5 dehydration of hexoses such as glucose leading to 5-hydroxymethylfurfural (HMF) is much more difficult.6–8 During the last few decades, many efforts have been made in order to improve the production of HMF from biomass.7 It is a versatile key intermediate for organic synthesis,9,10 production of fuels11,12 and for polymer chemistry.13

HMF formation from carbohydrate-containing biomass such as cellulose or starch involves three consecutive steps: (1) depolymerisation (2) glucose isomerisation to fructose and (3) fructose dehydration. The second step usually requires the use of a metal catalyst such as chromium, tin, vanadium or aluminate-based compounds.14–19

The efforts in HMF production were strongly affected by the development of ionic liquids (ILs) or deep eutectic solvents20,21 to dissolve biomass-based materials.22–25 Such media are often called “green solvents” but in order to assess greenness of ILs, synthesis, storage, recycling, and disposal have to be studied more profoundly.26 The main ionic liquids' limitation towards such industrial applications is related to the accurate control of purity and moisture.27 Another well-known solvent for HMF production is dimethylsulfoxide (DMSO). It is very effective for fructose-to-HMF conversion but it is completely inefficient for glucose or polysaccharide transformation.28–30 Sustainability or greenness of DMSO is controversially discussed because of its ability to carry almost any substance through the skin to more sensitive organs.31 Nevertheless, DMSO is currently used for cystitis treatment and studies are in progress on the effect of DMSO on arthritis and other diseases.31

As already pointed out, pure HMF is difficult to obtain and major problems of HMF large-scale production deal with its purification and extraction.9,30 To overcome those issues, many experimental tools were used such as biphasic systems8 and continuous reactive distillation.32

Another way to overcome HMF instability is its in situ conversion to 2,5-diformylfuran (DFF), which is also a promising platform molecule.33–35 Actually, DFF production is mainly carried out from pure HMF by metal-catalysed oxidation (NaV2O3, Ru/hydrotalcite, Pd, etc.) or from fructose after in situ dehydration.2,9,36 Recently, oxidation of HMF to DFF using heterogeneous photocatalysis with TiO2 was developed as a particularly sustainable process.37 Hitherto, no efficient one-pot synthetic method starting from glucose or polysaccharides has been reported.38,39

The well-known affinity of boric acid with polyols40–44 has been successfully used to isomerize glucose to fructose in IL.45–47 To the best of our knowledge, there is only one report on the use of boric acid in a more conventional solvent such as water.48 Herein, we report the use of boric acid, a sustainable non-metal reagent which is involved in many biological structures such as cell walls of green plants49 in DMSO for the efficient and direct HMF synthesis as well as its consecutive transformation into DFF.

Materials and methods

Chemicals and materials

All sugar reagents and DMSO were provided by Sigma-Aldrich and were used as received. Palatinose hydrate was purchased from TCI-chemicals and dried under vacuum at 40 °C for 4 days before use. NaBr and HMF were purchased from TCI Chemicals and used as received.

HPLC experiments were performed on Shimadzu Agilent 1200 series equipped with a nucleodur C18 column and a diode array detector. HPLC grade solvents were filtered and degassed before use. Sartorius 20 μm filters were purchased from VWR.

Typical experiment for the conversion of sugar to HMF or furfural

A round bottom flask equipped with a condenser was charged with carbohydrate (1 g), an appropriate amount of boric acid and DMSO (9 g). The mixture is stirred at 150 °C for an appropriate amount of time.

Typical one-pot sugar to DFF conversion experiment

A round bottom flask equipped with a condenser was charged with carbohydrate (1 g), an appropriate amount of boric acid, NaBr (0.3 eq. per glucose unit), formic acid (0.3 eq. per glucose unit) and DMSO (9 g). The mixture is stirred at 150 °C for an appropriate amount of time. DFF has also been isolated on a multigram scale by liquid/liquid extraction (see the ESI).

HMF; furfural and DFF analysis

After the specified time, 0.4 g of the reaction mixture was taken and diluted with deionised water (30 mL). This solution was filtrated before HPLC analysis.

HMF and DFF analyses were performed using an AcONa water solution (50 mM) at pH = 2.8 (adjusted by addition of AcOH) and acetonitrile (90/10 ratio) at a flow rate of 1 mL min−1 with a column temperature of 55 °C. HMF and furfural analyses were performed with 90/10 water/acetonitrile mixture at a flow rate of 0.6 mL min−1 at 25 °C. HMF, DFF and furfural amounts were determined using standard calibration curves.

Results and discussion

The influence of boric acid loading on the dehydration process of glucose to HMF (Fig. 1) was investigated. In the absence of boric acid, no HMF was formed, while in the presence of 0.5, 1 or 2 equivalents of this compound, yields up to 38% of HMF were observed. In the case of 0.5 and 1 equivalents, no decomposition of HMF took place before 8 h and 7 h, respectively. However, in the presence of 1 equivalent of boric acid and after 7 h, the yield decreased from 33 to 25% (Fig. 1). Another effect of the increase in boric acid loading is an increase in total acidity48 which favoured humin formation. In the case of less than 0.5 equivalent, a very slow conversion occurred. Similar results were obtained with ionic liquids as the solvent.45 Boric acid is essential for the isomerisation of glucose to fructose. A detailed mechanistic study based on DFT calculations has been recently published (Scheme 1).45 This study also involves the dehydration of fructose leading to the formation of HMF. Likewise, it was previously shown that the dehydration of fructose to HMF occurred in DMSO without addition of any catalyst.28 In this context, it should be mentioned that DMSO at high temperatures may form acidic species which also catalyse the dehydration.54,56
image file: c5re00004a-f1.tif
Fig. 1 Effect of boric acid loading on HMF yield in the transformation of glucose. Glucose (1 g; 5.6 mmol), boric acid (0.5, 1 or 2 eq.), DMSO (9 g), 150 °C.

image file: c5re00004a-s1.tif
Scheme 1 Simplified mechanism for the transformation of glucose into HMF.45

Carbohydrate concentration is well known to play an important role in HMF synthesis. We observed that the best results were obtained with 10% w/w glucose with respect to DMSO (Fig. 2). Higher concentrations lead to lower selectivities, probably because of the occurrence of polycondensation reactions which are generally favoured by higher monomer concentrations. Lower concentrations lead to almost the same yield. However, such conditions have no practical interest due to high solvent consumption. It should further be pointed out that after 8.5 h, no glucose was detected in the reaction mixture (NMR analysis).


image file: c5re00004a-f2.tif
Fig. 2 The effect of glucose concentration on HMF yield. Glucose (1 g; 5.6 mmol), boric acid (172 mg, 2.8 mmol), DMSO, 150 °C.

We applied the reaction conditions to the transformation of di- and polysaccharides as well as to the reaction of two pentoses (Table 1). Under the reaction conditions previously optimised, HMF was obtained with yields in the same order of magnitude of those from disaccharides (entries 2–5). The transformation of different starches yielded HMF in slightly lower yields (entries 6–8). However, in the case of potatoes and corn starches, the concentration of boric acid needed to be increased to 2 eq. per glucose unit (entries 6 and 7). The transformation of pure amylopectin is easier since it was successful under standard conditions, which may be explained by its amorphous structure (entry 8). Crystallinity acts as a physical barrier to chemical transformation. The low reactivity of the crystallite slows down the depolymerisation step. A reaction can only take place at the surface of the crystals. The reaction centres inside the crystals are not accessible to a reagent. Excess boric acid is believed to overcome the crystallinity effect, allowing a satisfactory yield of HMF. In these experiments (entries 6 and 7), a large amount of boric acid does not lead to significant degradation of HMF (compare Table 1 and its discussion). This observation may be explained by the fact that a part of the boric acid is bound to the polysaccharide which leads to its deactivation. These experiments thus highlight that boric acid also plays an important role in depolymerisation and decrystallisation processes. Only low amounts of HMF were formed in the transformation of microcrystalline cellulose under standard conditions. This result may be explained by the very low solubility and almost complete crystallinity of this polysaccharide.

Table 1 The transformation of various carbohydrates into HMF or furfural
Entry Carbohydratea Reaction Time (h) HMF yieldb (%) Furfural yieldb (%)
a Sugar (1 g), boric acid (172 mg, 2.8 mmol, 0.5 eq. per glucose unit), DMSO (9 g), 150 °C. b Yields were determined by HPLC. c Sugar (1 g), boric acid (762 mg, 12.3 mmol, 2 eq. per glucose unit), DMSO (9 g), 150 °C. d Sugar (2 g, 13.3 mmol), boric acid (412 mg, 6.6 mmol, 0.5 eq.) and DMSO (8 g) were used.
1 Glucose 8 35
2 Maltose 8 31
3 Sucrose 8 42
4 Palatinose 5 37%
5 Cellobiose 6 38%
6 Starch Potatoes 7 15a, 33c
7 Corn 6 30c
8 Amylopectin 7.5 29
9 Cellulose (MCC) 7.5 7c
10 Xylosed 8 35
11 Arabinosed 8 29


The dehydration of pentoses leading to furfural is well established5 and we also tested our reaction conditions for this transformation. Thus, the reaction of xylose and arabinose was performed in similar yields (entries 10 and 11). It should further be pointed out that in these cases, the sugar concentration can be doubled without diminishing the efficiency. This observation and the ease of the dehydration of pentoses are explained by the predominance of the furanose form in the equilibrium with the pyranose form in the case of these sugars.50

Application to primary biomass feedstock

We then applied our method to straw and bran as representative primary feedstock (Table 2). In order to lower mixture viscosity, the concentration of biomass had to be adjusted to 5% w/w instead of 10% w/w. Despite the large amounts of carbohydrates in straw, this material was completely unreactive and neither HMF nor furfural was detected. This may be explained by the high crystallinity index of straw cellulose.51 On the other hand, bran gave good yields of HMF and furfural. When starch was previously removed from bran, the HMF yield decreased probably because of the presence of more crystalline areas mainly attributed to the remaining cellulose.
Table 2 The transformation of primary biomass composition and conversiona
Glucose (%) Arabinose (%) Xylose (%) HMF yieldb (%) Furfural yieldb (%)
a Biomass (1 g), DMSO (19 g), boric acid (2 eq. per sugar unit), 150 °C. b Yields with respect to the initial composition were determined by HPLC. c Not detected.
Wheat straw 39, 3 30, 4 3, 6 ndc Ndc
Wheat bran 26, 5 9 17 25 19
Bran without starch 19 15, 8 29, 1 10 22


Our system provides a simple and versatile method for HMF and furfural synthesis with a satisfactory yield from carbohydrates. It allows one-pot deconstruction, isomerisation and dehydration without transition metal catalyst under standard conditions in DMSO.

One-pot DFF synthesis

DFF is usually synthesised from pure HMF with the use of metal catalyst in quantitative yield.52 However, those procedures do not consider the effect of impurities such as humins from the HMF synthesis. It has been proven that insoluble humins could inhibit HMF to furandicarboxylic acid (FDCA) oxidation.53 They have to be filtered off before further transformation. This result emphasised a heterogeneous catalysis limitation since humins completely inactivated the catalyst. Recently, a new and efficient procedure to synthesise DFF from fructose has been reported. Sodium bromide as a halide donor and DMSO as both solvent and oxidant are involved.54 Under these conditions, HMF is easily oxidised to DFF. This procedure is expected to be also efficient even in the presence of humins or other contaminant formed during sugar transformation.

We wonder whether these conditions may be combined with the improved isomerisation of glucose involving boric acid. First, we investigated the influence of the halogen source on the DFF yield (Table 3). In the case of NaCl (entry 1), only low quantities of DFF were formed while high amounts of HMF were detected. In the presence of NaBr (entry 2), substantial amounts of DFF were formed and no HMF was detected. It seems that this salt accelerates the oxidation of HMF to DFF. The better results obtained with NaBr may be explained by the higher nucleophilicity of the Br ion when compared to Cl (vide infra). The addition of NaI (entry 3) did not lead to an efficient formation of HMF or DFF. It is believed that active iodide compounds are generated and further oxidation or degradation may take place.54 As it was previously observed, formic acid is capable of catalysing fructose dehydration,55 we decided to study the influence of this acid in our reaction mixtures. Formic acid as a reductant also stabilises DMSO with respect to oxidative degradation at a high temperature.56

Table 3 The halogen effect on the formation of DFF
Entry Additivesa Reaction Time (h) DFF yieldb (%) HMF yieldb (%)
a Glucose (1 g, 5.6 mmol), boric acid (172 mg, 2.8 mmol), DMSO (9 g), NaX (0.3 eq.) and/or formic acid (63 μL, 1.7 mmol, 0.3 eq.), 150 °C. b Yields were determined by HPLC. c Not detected.
1 NaCl 24 8 38
2 NaBr 24 26 ndc
3 NaI 24 5 ndc
4 NaBr 17 16 7
5 NaBr, formic acidb 17 28 ndc
6 formic acidc 17 4 30


In order to improve comparability, we stopped the reaction after 17 h instead of heating for 24 h (Table 3, entries 4–6). Under these conditions and in the presence of NaBr, DFF was obtained in 16% yield from glucose (entry 4). In the presence of formic acid, DFF was formed in a relatively high yield (entry 5). When compared to the result in the absence of formic acid (entry 4), the formation of DFF was significantly accelerated. Since no HMF was detected at the end of the transformation after 17 h in the presence of formic acid (entry 5), we may suppose that formic acid also promote the oxidation of HMF to DFF (vide infra). It must further be pointed out that formic acid in the absence of NaBr was not able to promote this oxidation (entry 6).

Discussion on DFF formation mechanisms

Recently, it was discussed that the DMSO/NaBr system induces bromination of HMF and subsequent oxidation to DFF according to a Kornblum-like mechanism (Scheme 2, left part).54,57–59 Thus, HMF is transformed into bromoderivative 1. Addition of DMSO should lead to the formation of intermediate 2. Deprotonation and elimination of dimethylsulfide 3 then lead to the formation of DFF.
image file: c5re00004a-s2.tif
Scheme 2 Mechanism of the oxidation of HMF to DFF.

In order to check whether such a transformation may occur under our conditions, which involve the formation of 3 molecules of H2O resulting from the dehydration steps, 1 was prepared.60 It is known that the corresponding chloroderivative (5-chloromethylfurfural) rapidly undergoes hydrolysis.61 Indeed, when bromoderivative 1 was dissolved in DMSO containing 3 equivalents of water and heated at 60 °C for 2 hours, we observed fast and complete hydrolysis leading to the formation of HMF. At a higher temperature, the hydrolysis is almost instantaneous. Under those conditions, HBr is obviously formed but the equilibrium between HMF and 1 completely favoured HMF formation. We then explored a Swern-like reaction mechanism (Scheme 2, right part). The first step of the Swern reaction is DMSO activation usually through chlorosulfonium chloride synthesis. We synthesised62 its bromo analogue (bromosulfonium bromide 4) and compared its reactivity with the NaBr/DMSO system. When HMF is reacted with 4 in the presence of water at 150 °C, DFF is obtained.

In order to investigate the role of water in this system, we conducted anhydrous experiments. Interestingly, in the absence of water, 5-bromomethylfurfural 1 remained unreactive at 150 °C in DMSO. Furthermore, HMF reacts with NaBr/DMSO at 150 °C and leads to the formation of bromo compound 1 without DFF formation. When HMF is heated at 150 °C in anhydrous DMSO in the presence of 4, no DFF is formed and only 1 is detected. These results emphasised that in the absence of water, the equilibrium between 1 and 2 is favoured the formation of 1. Since the Kornblum and Swern reactions occurred only in the presence of bases,58,63,64 we may conclude that water acts as a base in the oxidation step.

The very fast hydrolysis of compound 1 and the similarity between NaBr/DMSO and bromosulfonium 4 lead us to suggest that the Swern reaction is the preferred pathway for DFF formation. We therefore suggest the following mechanism (Scheme 1, right part). HBr is formed from DMSO in the presence of sodium bromide under acidic conditions. HBr is then involved in the formation of bromosulfonium 4 (ref. 65) which reacts with HMF to form the oxosulfonium 2. In the presence of water, oxosulfonium 2 is deprotonated. The elimination of dimethylsulfide leads to DFF and HBr.

As already mentioned, the presence of formic acid has also a positive impact on the oxidation of HMF to DFF. Indeed, the presence of formic acid in the reaction mixture accelerates this oxidation and a quantitative yield of DFF is rapidly detected (Fig. 3). In order to check whether the formic ester of HMF undergoes transformation to DFF, this ester was synthesised66 and subjected to the reaction conditions. However, this HMF derivative was stable under these conditions. Furthermore, in the absence of formic acid, the transformation starts after an induction period. This period is shorter when formic acid is present in the reaction mixture. Since conversion of 2 to DFF takes place in the presence of water as base, formic acid is believed to be involved at the beginning of the reaction. We suggest that formic acid promotes the formation of bromodimethylsulfonium 4.


image file: c5re00004a-f3.tif
Fig. 3 The effect of formic acid on the direct conversion of HMF to DFF. *HMF (240 mg, 1.9 mmol), H2O (102 μL, 5.3 mmol), boric acid (118 mg, 1.9 mmol), NaBr (196 mg, 1.9 mmol), DMSO (9 g), 150 °C. **HMF (240 mg, 1.9 mmol), H2O (102 μL, 5.3 mmol), boric acid (118 mg, 1.9 mmol), NaBr (196 mg, 1.9 mmol), formic acid (72 μL, 1.9 mmol), DMSO (9 g), 150 °C.

Conclusions

We have developed the first one-pot production of 2,5-diformylfuran (DFF) from mono- and polysaccharides. The process has also been applied to the transformation of primary feedstock such as straw and bran. It involves monomerization, isomerisation of glucose to fructose, dehydration leading to 5-hydroxymethylfurfural (HMF) and finally selective oxidation to DFF. The process is efficient and environmentally friendly. Boric acid, sodium bromide and formic acid are used as reagents. The reactions have been carried out on a multigram scale in the laboratory (see the ESI). In order to further improve the degree of sustainability, the extraction and purification processes need to be optimised.

Acknowledgements

The authors gratefully acknowledge financial support from the Région Champagne-Ardenne and the European Union (FEDER) in the context of the project INNOBIOREF.

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Footnote

Electronic supplementary information (ESI) available: General methods; typical sugar to HMF or furfural conversion experiment; typical one-pot sugar to DFF experiment; HMF, furfural and DFF analysis; multigram DFF synthesis; synthesis of 5-(bromomethyl)furfural, bromodimethylsulfonium bromide and 5-(formyloxymethyl)furfural; hydrolysis of bromomethylfurfural; 1H and 13C NMR spectra. See DOI: 10.1039/c5re00004a

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