Sanny
Verma‡
a,
R. B. Nasir
Baig‡
a,
Mallikarjuna N.
Nadagouda
b,
Christophe
Len
c and
Rajender S.
Varma
*a
aSustainable Technology Division, National Risk Management Research Laboratory, U. S. Environmental Protection Agency, MS 443, Cincinnati, Ohio 45268, USA. E-mail: varma.rajender@epa.gov; Fax: +513- 569-7677; Tel: +513-487-2701
bWQMB, WSWRD, National Risk Management Research Laboratory, U. S. Environmental Protection Agency, Cincinnati, Ohio 45268, USA
cSorbonne Universités, Université de Technologie de Compiègne, Compiègne, France
First published on 31st October 2016
An organic sulfonated graphitic carbon nitride is synthesized and its application has been demonstrated in the conversion of carbohydrates into furanics and related value-added products. The most important feature of the material is the stability and acidity, which could be utilized at elevated temperatures for cleaving carbohydrates and converting them into biologically important scaffolds and platform chemicals.
Glucose and fructose are among the most abundant plant-derived carbohydrates.5 They have been converted into building blocks for the synthesis of value-added chemicals used in drug discovery and in the synthesis of polymers among other industrial applications.6 In general, these carbohydrates are heated with mineral acids to convert them into 5-hydroxymethylfurfural (HMF) and levulinic acid notwithstanding some limitations in terms of product yields and experimental conditons.7 Researchers are incessantly investigating pathways to achieve higher yields by reconnoitring a wide range of homogenous and heterogeneous catalysts8 using ionic liquids9 and biphasic systems.10 Heterogeneous and homogeneous catalysis8 have shown limited success in terms of productivity, yield and cost-efficiency. The quest for identification of a highly acidic and relatively benign material that could efficiently accomplish the conversion of carbohydrates to furanics with a recyclability attribute has been a challenge.11 Heterogeneous organo-catalysis is probably an ideal choice as it does not involve the use of any metals.12 Cao et al. reported the use of ammonium resin to convert glucose in to HMF.13 However, this reaction required high temperature (140 °C) along with an aqueous–organic solvent (70% DMSO in water) with a maximum yield of 56%. Bhaumik et al. used sulfonated triphenylaniline polymer as an acidic organo-catalyst14 wherein the catalyst preparation required the use of toxic triphenylaniline, polymerization under anhydrous conditions followed by a sulfonation step. Furthermore, the high temperature and requirement of anhydrous DMSO have limited the wider scope of this reaction. In continuation of our focus on the development of sustainable methods,15 herein, we report a heterogeneous organo-acid catalyst derived from the electron-rich graphitic carbon nitride for the conversion of carbohydrates into value-added platform chemicals (Scheme 1).
The synthesized catalyst was characterized using scanning electron microscopy (SEM), transmission electron microscopy (TEM), X-ray diffraction (XRD), Fourier transform infrared spectroscopy (FTIR) and solid state 13C NMR. The SEM (Fig. 1a and b), TEM (Fig. 1c and d) and XRD (Fig. 2) of graphitic carbon nitride (g-CN) and sulfonated graphitic carbon nitride (Sg-CN) show a visible difference in morphology and crystalline nature. The SO3H-immobilized Sg-CN becomes crystalline, whereas before immobilization, g-CN was amorphous in nature.
The FTIR (Fig. 3) and solid state 13C NMR (Fig. 4) confirm the functionalization of graphitic carbon nitride surface. The presence of strong absorption between 1190 and 1170 cm−1 and 1020 and 1040 cm−1 confirms the presence of the –SO3H moiety in Sg-CN. The different pattern is due to a change in the electronic environment after sulfonation. For the 13C NMR spectra of graphitic carbon nitride and sulfonated graphitic carbon nitride, the peak at 140 ppm is the characteristic signal for sulfonated graphitic carbon nitride (Sg-CN), which is affirmed by FTIR of g-CN and Sg-CN. The stability of Sg-CN was examined using thermogravimetric analysis (TGA). The TGA analysis curve of sulfonated graphitic carbon nitride (Sg-CN) confirmed that the catalyst is stable up to ∼250 °C as negligible weight loss (<3%) was observed in the TGA (Fig. 5). The immobilization of the sulfonic group was further confirmed by BET surface analysis of the sulfonated graphitic carbon nitride (10.04 m2 g−1, ESI†) and graphitic carbon nitride (35.42 m2 g−1, ESI†). After the immobilization, –SO3H ion goes and sits inside the pores via ionic interaction with the nitrogen lone pairs. A comparison of adsorption and desorption curves for g-CN (ESI, Fig. S7 and S8†) and Sg-CN (ESI, Fig. S5 and S6†) clearly indicates that the SO3H ions are sitting in the pores and binding with the nitrogen in Sg-CN. Due to this, the nature of g-CN changes from amorphous to crystalline in Sg-CN, which results in better packing and consequently a decrease in the total surface area although the pore distribution remains uneven.
The immobilization of –SO3H is confirmed by the presence of sulfur in the energy-dispersive X-ray (EDX) spectrum (ESI, Fig. S9†) and further supported by the X-ray photoelectron spectrum (XPS) of Sg-CN (Fig. 6). The exact concentration of sulfur was determined using elemental analysis and found to be 5.47 mmol g−1. The higher acidity strength of the Sg-CN catalyst was anticipated due to the positive charge developed on the nitrogenous framework after the –SO3H immobilization.
Entry | Solvent | Temperture (°C) | Time | Yieldb |
---|---|---|---|---|
Reaction conditions:a Xylose (2 mmol), Sg-CN (50 mg).b Isolated yield.c 25 mg of Sg-CN used.d 12.5 mg of Sg-CN used. | ||||
1 | DMSO | 25 | 24 h | <3% |
2 | DMSO | 50 | 8 h | 60% |
3 | DMSO | 100 | 25 min | 95% |
4 | DMF | 100 | 1 h | 30% |
5 | Dioxane | 100 | 1 h | 10% |
6 | Acetonitrile | 82 | 1 h | trace |
7 | Ethanol | 78 | 1 h | 9% |
8 | Methanol | 65 | 1 h | 10% |
9 | Water | 100 | 30 min | 95% |
10c | Water | 100 | 30 min | 96% |
11d | Water | 100 | 4 h | 86% |
After optimizing the reaction conditions, we embarked on the applications of sulfonated graphitic carbon nitride (Sg-CN). In order to make broader use of this methodology, we added 1,2-phenylenediamine to the reaction mixture, which directly gave the pharmaceutically important benzimidazole derivative in 84% yield (Scheme 2).
The success of Sg-CN-catalyzed conversions of xylose into value-added platform chemicals motivated us to expand further the prospects and applications of this catalyst. Consequently, we treated fructose with sulfonated graphitic carbon nitride under similar conditions, leading to the formation of the corresponding 5-hydroxymethylfurfural (HMF) in very good yield (Scheme 3). Utilizing a one-pot protocol, KBr, Sg-CN catalyst and fructose afford a 94% yield of 2,5-diformylfuran (DFF) via in situ oxidation of HMF (Scheme 4). KBr serves as an internal oxidant that oxidizes HMF in situ, leading to the selective formation of DFF. Replacement of KBr oxidant with DMSO, which may also serve as an oxidant,13 resulted in no formation of desired product. Interestingly, the use of KBr in conjunction with DMSO afforded predominantly 5-methylsulfanylmethyl-furan-2-carbaldehyde with a minor amount of DFF (95:5 ratio; Scheme 3), the thiolated compound being the major product. In most of the documented results under similar conditions, DFF was the sole product described with occasional traces of 5-methylsulfanylmethyl-furan-2-carbaldehyde.13,18 However, herein, the reaction of fructose with Sg-CN afforded the selective formation of 5-methylsulfanylmethyl-furan-2-carbaldehyde with insertion of methylsulfide (CH3S–) in very high yields (Scheme 3). This unprecedented formation of 5-methylsulfanylmethyl-furan-2-carbaldehyde is an important finding, missing in earlier explorations. Interestingly, heating the aqueous solution of fructose/glucose with Sg-CN in a sealed tube over a longer period of time (8 h) at 150 °C provided levulinic acid (Scheme 4). Levulinic acid is an important intermediate of use in the synthesis of basic building blocks such as γ-valerolactone and many natural products.19
The plausible mechanisms for the dehydration of xylose and fructose have been proposed in Schemes 5 and 6, respectively. The dehydration of xylose to furfural takes place via the formation of 2,5-anhydroxylose furanose cyclic intermediate I20 and dehydration of fructose to HMF via an enol tautomerization intermediate.21
It was imperative to evaluate the stability of the catalyst in recycling experiments using fructose as the model substrate. The reaction of fructose in water at 100 °C gave the formation of HMF. After the reaction, the catalyst was separated by filtration/centrifugation, washed with acetone and re-used for the next cycle with the fresh reactants. The catalyst was found to be active even after three cycles, clearly indicating that it does not lose its activity during the course of reaction (ESI, Fig. S1†). The SEM, TEM and XRD of the recycled catalyst showed that it retained its morphology and crystalline nature (ESI†), which is in corroboration with the outcome of the recycling experiments.
Footnotes |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/c6gc02551j |
‡ Equal contribution. |
This journal is © The Royal Society of Chemistry 2017 |