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Research / 2019 / Article

Research Article | Open Access

Volume 2019 |Article ID 6262719 |

Zhen-Yu Wu, Peng Yin, Huan-Xin Ju, Zhi-Qin Chen, Chao Li, Si-Cheng Li, Hai-Wei Liang, Jun-Fa Zhu, Shu-Hong Yu, "Natural Nanofibrous Cellulose-Derived Solid Acid Catalysts", Research, vol. 2019, Article ID 6262719, 11 pages, 2019.

Natural Nanofibrous Cellulose-Derived Solid Acid Catalysts

Received30 Nov 2018
Accepted27 Jan 2019
Published16 Apr 2019


Solid acid catalysts (SACs) have attracted continuous research interest in past years as they play a pivotal role in establishing environmentally friendly and sustainable catalytic processes for various chemical industries. Development of low-cost and efficient SACs applicable to different catalysis processes are of immense significance but still very challenging so far. Here, we report a new kind of SACs consisting of sulfonated carbon nanofibers that are prepared via incomplete carbonization of low-cost natural nanofibrous cellulose followed by sulphonation with sulfuric acid. The prepared SACs feature nanofibrous network structures, high specific surface area, and abundant sulfonate as well as hydroxyl and carboxyl groups. Remarkably, the nanofibrous SACs exhibit superior performance to the state-of-the-art SACs for a wide range of acid-catalyzed reactions, including dimerization of α-methylstyrene, esterification of oleic acid, and pinacol rearrangement. The present approach holds great promise for developing new families of economic but efficient SACs based on natural precursors via scalable and sustainable protocols in the future.

1. Introduction

Acid catalysis plays a crucial role in many industrial chemical processes, such as fine-chemical synthesis, oil refining, and biomass conversions [17]. Traditional liquid acid catalysts, e.g., H2SO4, HCl, H3PO4, and HF, are highly efficient and widely used in these processes [2, 5, 7, 8]. Nevertheless, liquid acid catalysts suffer from problems of safety threat, corrosivity to equipments, catalyst waste, and difficulty of separation and recovery, which significantly limit their practical applications [24, 8]. The principles of green and sustainable chemistry stimulate the replacement of the homogeneous liquid acid catalysts with heterogeneous solid acid catalysts (SACs) with inherent advantages of being safe, environmentally friendly with respect to corrosiveness, less waste, and ease of separation and recovery [2, 5, 810]. Yet the catalytic performance of the state-of-the-art SACs, such as heteropolyacids, metal oxides (e.g., niobic acid), phosphates, zeolite (e.g., H-Mordenite), and sulfonated resins (e.g., Amberlyst-15, nafion) [1, 8], needs to be significantly improved owing to their low densities of acid sites, poor stability, and high cost [7, 8].

To this end, some novel SACs, such as phenylene-sulfonic acid functionalized ethenylene-silica [11], sulfonated polymers [12], carbon-silica composites [13, 14], and carbon-based materials [1522], have been developed recently and showed promising performance for various acid-catalyzed reactions. A particularly important contribution to this field is the development of carbonaceous SACs by the sulfonation of incompletely carbonized D-glucose and sucrose by Hara et al. [16]. The incompletely carbonized carbohydrates with flexible polycyclic carbon frameworks and large amount of oxygen-based groups are beneficial to the followed sulfonation process [4, 16, 18, 20, 23]. As a result, the prepared SACs contain abundant -SO3H acid sites as well as high density of hydrophilic functional groups and thus show good catalytic performance in some hydrophilic reactions, such as hydration, hydrolysis, and esterification reactions [4, 16, 18, 20, 23]. However, the low specific surface area and poor porosity of carbohydrate-derived carbonaceous SACs hinder the diffusion of hydrophobic reactants to active acid sites and therefore result in poor even no catalytic activity of these catalysts for hydrophobic reactions [13, 2426]. Developing carbon-based SACs with high -SO3H density, porous nanostructure, and large specific surface area is therefore highly desirable but challenging to promise these catalysts applicable to both hydrophilic and hydrophobic reactions as well as other important reactions [2426].

Herein, we report a new type of highly porous carbon-based SACs that are prepared via a two-step process of carbonization and sulfonation of natural nanofibrous cellulose. Owing to the low-cost natural cellulose precursor and simple preparation process, our method is environmentally friendly, inexpensive, and easy to scale up. Importantly, the prepared SACs well inherit the three-dimensional (3D) nanofiber network structure of natural cellulose precursor and thus exhibit high specific surface areas (up to 837 m2 g−1) and large pore volumes (up to 0.92 cm3 g−1); the efficient sulfonation process endows the nanofibrous SACs with abundant Brönsted acid sites including -SO3H groups (up to 2.42 mmol g−1) as well as hydroxyl (-OH) and carboxyl (-COOH) groups (total acid density of up to 3.88 mmol g−1). As a result, in a wide range of important acid-catalyzed reactions, including dimerization of α-methylstyrene (AMS, a hydrophobic acid-catalyzed reaction), esterification of oleic acid (a hydrophilic acid-catalyzed reaction), and pinacol rearrangement (an acid strength-dependent reaction), our nanofibrous SACs exhibit much better performance than the state-of-the-art SACs, e.g., Amberlyst-15, H-Mordenite and niobic acid, and in some cases even better than H2SO4 under similar reaction conditions.

2. Results

2.1. Preparation and Structural Characterizations of Nanofibrous SACs

We recently demonstrated two kinds of natural nanofibrous celluloses, i.e., bacterial cellulose (BC) and wood-based nanofibrillated cellulose (NFC), as ideal precursors for preparation of carbonaceous nanofiber aerogels [2729]. BC, a low-cost biomass consisting of 3D nanofibrous cellulose network that can be now produced on an industrial scale via a microbial fermentation process [27], was selected as a typical precursor in this work for preparing nanofibrous SACs. The preparation of nanofibrous SACs involves a two-step process of (1) carbonization of BC aerogels at 400-800°C under a N2 atmosphere to generate carbon-based nanofibers (BC-CNFs) aerogels and (2) subsequent sulfonation of the BC-CNFs with concentrated H2SO4 or fuming H2SO4 (Figure 1(a)). The obtained catalysts are denoted as BC-CNFs-x-SO3H or BC-CNFs-x-SO3H, where is the pyrolysis temperature and asterisk indicates the SACs prepared with fuming H2SO4. The commercial availability of low-cost BC precursors and simple preparation processes allow BC-CNFs-SO3H catalysts to be easily scaled up (Figures 1(b) and 1(c)). Scanning electron microscopy (SEM) and transmission electron microscopy (TEM) images clearly indicate that the nanofibrous network structures of original BC precursors are kept well in all of the BC-CNFs--SO3H and BC-CNFs--SO3H catalysts even after carbonization and harsh sulfonation processes (Figures 1(d) and 1(e) and Figures S1-S4). The effective sulfonation is roughly confirmed by energy dispersive X-ray spectroscopy (EDS) spectra (Figure S5). The corresponding elemental mapping images show that S and O species are homogeneously distributed throughout the individual nanofiber as well as the whole nanofibrous network structure (the insets of Figure 1(e) and Figures S6-S8), implying that -SO3H groups have been successfully grafted onto BC-CNFs and were uniformly distributed within the whole nanofibrous network. The XRD patterns of BC-CNFs--SO3H show broad but weak diffraction peaks (2θ = 10-30°, Figure S9), indicating the amorphous carbon structure composed of aromatic carbon sheets in a considerably random fashion, which is consistent with Raman analysis results (Figure S10) [18].

N2 sorption measurements were performed to investigate the textural properties of BC-CNFs-SO3H SACs and the results were summarized in Table 1 and Figures S11 and S12. All of BC-CNFs-x-SO3H SACs show high specific surface area ranging from 496 to 837 m2 g−1 and large pore volume ranging from 0.41 to 0.92 cm3 g−1. These values are much higher than those of previously reported biomass-derived SACs, such as D-glucose [23], sucrose [16], and microcrystalline cellulose derived SACs [18]. Note that the sulfonation with concentrated H2SO4 did not damage the porous structure of BC-CNFs, while the fuming H2SO4 sulfonation led to a distinct decrease of specific surface area; the specific surface area considerably dropped from 512 m2 g−1 for BC-CNFs-400 to 192 m2 g−1 for BC-CNFs-400-SO3H. Additionally, the pore size distribution analysis manifests the presence of a large number of mesopores for BC-CNFs-SO3H SACs (Figures S11 and S12). As far as we know, this work represents the first case of preparing SACs with high specific surface area and large pore volume from biomass precursors without templating or activation processes.

CatalystSpecific surface area (m2 g−1)Pore volume
(cm3 g−1)
Total acid density
(mmol g−1
SO3H density
(mmol g−1

Nafion R-1100<1/1.131.02
Niobic acid1240.020.41/

Total acid density is determined by acid-base back titration; SO3H densities are estimated from the S content in sample compositions determined by elemental analysis.
2.2. Surface Chemistry Characterization of Nanofibrous SACs

We then carried out the Fourier transform infrared spectroscopy (FT-IR), 13C magic angle spinning nuclear magnetic resonance (13C MAS NMR), acid-base back titration, X-ray photoelectron spectroscopy (XPS) and X-ray absorption spectroscopy (XAS) analyses to reveal the detailed surface chemistry of the nanofibrous SACs.

Figure 2(a) shows the FT-IR spectra of BC-CNFs-400 before and after sulfonation. For BC-CNFs-400, the peaks at 3000-3700 cm−1, 2880-2990 cm−1 and 1350-1400 cm−1 are assigned to O-H, C-H and aromatic C-O stretching vibrations, respectively [30]; The peaks at 1700 cm−1 and 1500-1670 cm−1 are attributed to C=O and C=C stretching vibration, respectively [30]. The rich oxygen-containing groups in BC-CNFs-400 are beneficial to followed sulfonation processes. After sulfonation, three new peaks at 1338 cm−1, 1065 cm−1 and 658 cm−1 attributed to -SO3H groups emerge in the FT-IR spectrum of BC-CNFs-400-SO3H [18, 30]. The surface functional groups on the nanofibers were further analyzed by 13C MAS NMR (Figure 2(b) and Figure S13). The peaks at 128, 155, and 182 ppm assignable to polycyclic aromatic carbon atoms, phenolic OH, and COOH groups are found in the both 13C MAS NMR spectra of BC-CNFs-x and BC-CNFs-x-SO3H as well as BC-CNFs-400-SO3H [13, 18, 23]. Meanwhile, all of BC-CNFs-SO3H SACs exhibit a shoulder peak at 140 ppm, which belongs to the aromatic carbon with SO3H groups (Ar-SO3H, ca. 140 ppm) [23, 24]. The abundant oxygen-containing groups make these nanofibrous SACs have an excellent hydrophilic property (Figure S14).

Further, the total acid density (referring to total H+ number per gram of Brönsted acids, i.e., the total density of SO3H, COOH, and OH groups) of the nanofibrous SACs was estimated by acid-base back titration method; the SO3H density was determined by elemental analyses based on the fact that sulfur element exclusively came from -SO3H group in the nanofibrous SACs. The results of the nanofibrous SACs as well as H2SO4 and several reference SACs were summarized in Table 1. The BC-CNFs-400-SO3H possesses a high total acid density of 1.84 mmol g−1 and SO3H density of 0.85 mmol g−1, comparable to that of Nafion R-1100 (1.13 mmol g−1 and 1.02 mmol g−1, respectively). With the increase of carbonization temperature, the total acid density and SO3H density drop dramatically for BC-CNFs-600-SO3H and BC-CNFs-800-SO3H because of the increased difficulty in sulfonation for the carbons with higher carbonization degree [24]. Of note, BC-CNFs-400-SO3H∗ prepared with fuming H2SO4 sulfonation exhibits a much higher total acid density of 3.88 mmol g−1 and SO3H density of 2.42 mmol g−1; the SO3H density surpasses most of reported carbon-based SACs [13, 1619, 2326] and even can compete with Amberlyst-15 with a high SO3H density of 4.36 mmol g−1.

The surface composition and chemical state of the constituent elements of BC-CNFs-x and corresponding SACs were additionally characterized by XPS (Figures 2(c)–2(f) and Figure S15). The C1s spectrum of BC-CNFs-400 can be deconvoluted into four peaks at 284.8 eV, 285.5 eV, 286.7 eV, and 288.8 eV corresponding to C-C and/or C=C, C-O, C=O, and COOH, respectively (Figure 2(d)) [31, 32]. Interestingly, the intensity of C=O and COOH peaks increases obviously in BC-CNFs-400-SO3H, probably because of the oxidization of carbon during the sulfonation process. In the high-resolution O1s spectra, the peaks at 531.5 eV and 533.4 eV in BC-CNFs-400 are assigned to oxygen atoms in C=O and C-O, respectively (Figure 2(e)) [30]. A new O1s peak centered at 532.6 eV appears for BC-CNFs-400-SO3H, which can be attributed to oxygen atoms in -SO3H groups [30]. The high-resolution S2p spectrum of BC-CNFs-400-SO3H can be deconvoluted into two peaks at 167.6 eV and 168.7 eV (Figure 2(f)), corresponding to S2p3/2 and S2p1/2 in -SO3H groups, respectively [30]. No other sulfur-containing configurations are observed by XPS analyses. The XPS of other nanofibrous SACs were also analyzed and the results were presented in Figure S15.

XAS can probe unoccupied electronic states and is particularly sensitive to the local electronic configuration. XAS measurements of C, O, and S K-edge were therefore performed to further investigate the electronic structure of the nanofibrous SACs. The C K-edge XAS spectra of BC-CNFs-400 and BC-CNFs-400-SO3H clearly show the presence of unoccupied π∗ (1s→π∗) and σ∗ (1s→σ∗) states at around 284.9 and 292.1 eV, respectively, indicating the aromaticity of both samples (Figure 2(g)) [33]. However, no recognizable structures can be identified between 293 and 310 eV, probably because the amorphous nature of these two samples induces a spread of the σ∗ resonances [34]. The peaks at photon energies of 285.7, 286.3, and 288.7 eV are associated with various functional oxygen-containing groups in BC-CNFs-400 and BC-CNFs-400-SO3H [33, 34]. The peaks of a1, a2, and a3 correspond to the π∗ resonances of carbons being in a chemical bond with oxygen in hydroxyl groups (C-OH), carbons in epoxy groups (C-O-C), and carbons in the double bonds (C=O) in carbonyl and carboxyl (C=O, COOH), respectively [3335]. Remarkably, the peak of a3 of BC-CNFs-400-SO3H is much sharper and stronger than that of BC-CNFs-400, indicating much increased contents of carbonyl and carboxyl groups after sulfonation, agreeing with the XPS results well. The O K-edge XAS spectra further reveal the changes of surface chemistry during sulfonation process. BC-CNFs-400 and BC-CNFs-400-SO3H show very similar peaks at 531.8 (b1), 536.0 (b3) and 540.5 eV (b5), which can be assigned to the π∗ resonance of C=O/COOH bonds, σ∗ resonances of C-OH bonds and C=O/COOH bonds, respectively (Figure 2(h)) [35, 36]. Two new peaks at photon energies of 532.9 and 537.5 eV emerge at O K-edge XAS spectrum of BC-CNFs-400-SO3H, which is associated with the π∗ and σ∗ resonances of -SO3H groups [37]. Finally, the S K-edge XAS spectra directly reveal the successful sulfonation: BC-CNFs-400-SO3H displays a peak at 2481.2 eV that is assigned to -SO3H groups with S in the +6 state [38], while BC-CNFs-400 has no peak at 2470-2495 eV (Figure 2(i)). The C, O, and S K-edge of other nanofibrous SACs were also tested and carefully analyzed; all of them exhibit similar results with BC-CNFs-400-SO3H (Figure S16).

Overall, the above FT-IR, 13C MAS NMR, acid density test, and XPS and XAS analyses indicate unambiguously that sulfonation can efficiently endow the incompletely carbonized natural nanofibrous cellulose with abundant -SO3H groups and other oxygen-containing groups, meanwhile maintaining the nanofibrous structures and high specific surface areas.

2.3. The Performance of Acid-Catalyzed Reactions

Three different but highly important acid-catalyzed liquid-phase reactions were selected for evaluating the catalytic performance of our nanofibrous SACs, including a hydrophobic acid-catalyzed reaction (dimerization of AMS), a hydrophilic acid-catalyzed reaction (esterification of oleic acid with methanol), and an acid strength-dependent reaction (pinacol rearrangement). H2SO4 and several state-of-the-art SACs, i.e., Amberlyst-15, Nafion R-1100, H-ZSM-5, H-mordenite, and niobic acid, were also tested under the same conditions for comparison.

2.4. Catalytic Dimerization of AMS

The dimerization of AMS produces valuable unsaturated dimers (2,4-diphenyl-4-methyl-1-pentene and 2,4-diphenyl-4-methyl-2-pentene) accompanied with an undesirable saturated dimer (1,1,3-trimethyl-3-phenylindan) [13, 25]. The unsaturated dimers are industrially important chemicals in the syntheses of styrene-butadiene-rubber and acrylonitrile-butadiene-styrene resin; thus it is necessary to selectively synthesize the unsaturated dimers by inhibiting the formation of the saturated dimer [13, 25]. H2SO4 gave a nearly 100% conversion but a very poor selectivity; 95.7% AMS was converted into the undesirable saturated dimer (Table 2). The time courses of conversion and yield tests show that most of AMS was rapidly converted into unsaturated and saturated dimers during 0.5 h over H2SO4. Unfortunately, the unsaturated dimers were gradually converted into saturated dimers at following reaction process; finally the yield of unsaturated dimers was decreased to 4.3% after 20 h (Figure S17a), indicating that the intramolecular Friedel-Crafts alkylation proceeded continuously over H2SO4. As a conventional resin-based strong solid acid, Nafion R-1100 with high density of SO3H groups could not efficiently catalyze the AMS dimerization, which is associated with its low specific surface area [13], while Amberlyst-15 with relatively large surface area exhibited a superior catalytic conversion of 98.8% but a low selectivity of 56.3% for unsaturated dimers (Table 2). The whole reaction process of the dimerization of AMS for Amberlyst-15 was very similar to that of H2SO4 (Figure S17b), but its reaction speed was much slow than that of H2SO4, probably because of its low SO3H density. In addition, H-ZSM-5, H-Mordenite and niobic acid with acidic OH groups also displayed negligible catalytic activity for the dimerization of AMS (lower that 10% conversion).

EntryCatalystConversion (%)Selectivity (%)
Unsaturated dimersSaturated dimers

6H2SO4ca. 1004.3095.7
8Nafion R-1100TraceTraceTrace
11Niobic acidTraceTraceTrace

,4-diphenyl-4methyl-1-pentene and 2,4-diphenyl-4-methyl-2-pentene; ,1,3-trimethyl-3-phenylindan.

Remarkably, when the BC-CNFs-x-SO3H catalysts were tested, they showed remarkable catalytic performance for the AMS dimerization. Particularly, the conversion of AMS and selectivity for unsaturated dimers could reach 96.3% and 96.8% for BC-CNFs-400-SO3H and 92.9% and >99% for BC-CNFs-600-SO3H after 20 h (Table 2). The much higher selectivity of BC-CNFs-x-SO3H to the unsaturated dimers over H2SO4 and Amberlyst-15 is probably due to the blocking of intramolecular Friedel-Crafts alkylation on BC-CNFs-x-SO3H enriched with phenolic OH groups (Figure S17c) [25]. Indeed, the incorporation of p-cresol in the H2SO4-catalyzed AMS dimerization could distinctly improve the selectivity to unsaturated dimers (Figure S18). Of note, when using microcrystalline cellulose and glucose derived SACs (i.e., cellulose-600-SO3H and glucose-600-SO3H) with low specific surface area of <1 m2 g−1 for catalyzing the dimerization of AMS, very low activity (lower than 5% conversion) was observed despite their high total acid density and SO3H density (Figures S17d and S19). These results clearly manifest the vital role of the high porosity resulting from the nanofibrous structure of BC-CNFs-x-SO3H in hydrophobic acid-catalyzed reaction.

The reusability of BC-CNFs-600-SO3H for AMS dimerization was evaluated by a simple decantation method (Figure S20). No obvious decrease in activity and selectivity was observed after three reuses of the same sample, though the activity decreased in the fourth cycle. We found that the nanofibrous microstructure of BC-CNFs-600-SO3H was well retained (Figure S21), but the total acid density dropped to 0.51 mmol g−1, which should be an important reason for the catalytic performance degradation. Besides, the blocking of active SO3H groups by adsorbed reactants and/or products and the unavoidable catalyst loss during the recycle process should be considered as other reasons for the decrease of catalytic performance [25, 39].

2.5. Catalytic Esterification of Oleic Acid with Methanol

The esterification of fatty acids with methanol was selected to further demonstrate the wide applicability of BC-CNFs--SO3H for various acid-catalyzed reactions (Table 3). The esterification of fatty acids with alcohols to produce fatty acid esters is an important step in the production of biodiesel, which is considered a promising alternative fuel to replace petroleum-based fuels because of its biodegradability, nontoxicity, and favorable combustion emission profile [4, 16, 22]. Methyl oleate was only product detected by gas chromatography in this acid-catalyzed liquid-phase reaction. When three conventional SACs including H-ZSM-5, H-Mordenite, and niobic acid which are free of -SO3H were used for esterification of oleic acid with methanol, the conversion of oleic acid was very low (<15%) after 6 h reaction and the corresponding turnover frequencies (TOFs) were less than 1 h−1. Under the same conditions, Nafion R-1100 with high SO3H density also showed a poor activity, while Amberlyst-15 with higher SO3H density and larger specific surface area gave a moderate activity with a conversion of 42.4% and a TOF of 8.86 h−1. Remarkably, BC-CNFs-400-SO3H and BC-CNFs-600-SO3H with relatively low SO3H density even exhibited much better catalytic performance; ca. 90% oleic acid was converted on them within 12 h and their TOFs are more than 15.0 h−1. The higher catalytic activity of BC-CNFs-SO3H over Nafion R-1100 and Amberlyst-15 is attributed to not only their high specific surface areas but also the flexibility carbon structures with large amounts of hydrophilic functional groups that provide access for the reactant molecules to the active SO3H groups inside the carbon matrix [18, 23]. As expected, H2SO4, as a homogeneous acid catalyst, had the highest activity with a conversion of 98.3% and a TOF of 41.6 h−1. When BC-CNFs-400-SO3H∗ with higher SO3H density (nearly triple of that in BC-CNFs-400-SO3H) which was prepared by fuming H2SO4 sulfonation was used for this esterification reaction, it showed nearly the same conversion and comparable TOF (29.3 h−1) as the high-performance H2SO4 catalyst. Furthermore, BC-CNFs-400-SO3H could be well recycled for four times without obvious performance degradation (Figure S22).

EntryCatalystConversion (%)TOF (h−1)

8Nafion R-110013.20.48
11Niobic acid13.30.21

TOF is calculated by the conversion of oleic acid per acid site per hour with conversion less than 40%; the active sites are defined as H+ measured by acid-base titration method.
2.6. Catalytic Pinacol Rearrangement

Pinacol rearrangement is a valuable process for synthesizing aldehydes or ketones through the skeletal rearrangement of 1,2-diols and elimination of water [40]. The reaction involves the evolution of a cationic intermediate, which is stabilized under highly acidic conditions [11]. We therefore selected this reaction to show the association of acid strength of the BC-CNFs-SO3H catalysts with their catalytic performance (Table 4). H-ZSM-5, H-Mordenite, niobic acid, and Nafion R-1100 showed very poor conversion (lower that 10%), as results of their low acid strength. In contrast, all of BC-CNFs-SO3H catalysts exhibited high performance for pinacol rearrangement with >85% conversion and >70% selectivity for pinacolone. The BC-CNFs-400-SO3H catalyst could be recycled for three times with a slight performance degradation (Figure S23). Particularly, BC-CNFs-400-SO3H∗ showed a conversion of 99.4% and a selectivity for pinacolone of 81.9%, which is very close to H2SO4 and exceeds Amberlyst-15. The high acid strength of BC-CNFs-400-SO3H∗ was verified by 31P MAS NMR tests (Figure S24).

EntryCatalystConversion (%)Selectivity (%)

6H2SO4ca. 10086.513.5
8Nafion R-11003.2037.562.5
11Niobic acidTraceTraceTrace

2.7. Catalytic Performance for Other Reactions

Besides being used for the above acid-catalyzed reactions, the BC-CNFs-SO3H catalysts were also explored for other liquid-phase reactions, including the synthesis of β-enamino ketones/esters and hydrogenation of nitrobenzene. Enamination of β-dicarbonyl compounds, an important and widely used transformation, can form β-enamino ketones and esters [41, 42]. The obtained compounds are a highly versatile class of intermediates for the synthesis of heterocycles and biologically active compounds [41]. Various amines (aromatic, cyclic, and aliphatic) and β-diketones or β-ketoesters were investigated for synthesizing β-enamino ketones/esters in the presence of BC-CNFs-400-SO3H (Table S1). Most yields of β-enamino ketones/esters exceeded 90%, which was close comparable with the results of reported metal-based catalysts [41]. The relatively low yield (52.5%) of the reaction between acetylacetone and o-chloroaniline probably results from the stereo-hindrance effect. The high catalytic performance of BC-CNFs-400-SO3H for synthesis of β-enamino ketones/esters is believed to be associated with high solid acid groups and active defect sites [42]. In addition, BC-CNFs-400-SO3H also exhibited promising activity for catalyzing the hydrogenation of nitrobenzene. Using N2H4·H2O as the reductant, nitrobenzene could completely converted into aniline over BC-CNFs-400-SO3H with a superior yield of 99.6%, which suppresses most of the reported carbon-based catalysts (Table S2). The BC-CNFs-400-SO3H catalyst could be well recycled; only a slight activity decrease (ca. 8%) was observed after 5 runs of catalytic reactions (Figure S25), demonstrating good reusability as a heterogeneous carbon-based catalyst.

These catalysis tests clearly confirm the distinct advantages of BC-CNFs-SO3H SACs over H2SO4 and the state-of-the-art SACs in a wide range of liquid-phase acid-catalyzed reactions. The high performance of BC-CNFs-SO3H SACs is associated with their unique nanofibrous network structure, abundant functional groups, high -SO3H density, and acid strength. Another superiority of BC-CNFs-SO3H catalysts is easy to scale up due to the commercially available low-cost biomass precursors and simple preparation processes. Particularly, the more sustainable and cheaper wood-based NFC could also be employed as precursor to prepare efficient nanofibrous SACs (Figure S26). Moreover, our developed method can also be extended to other nanofibrous SACs, such as phosphorylated BC-CNFs (Figure S27).

3. Discussion

In summary, we report a facile, low-cost, and scalable method to prepare a new type of nanofibrous SACs by incomplete carbonization and sulfonation of natural nanofibrous celluloses. The prepared nanofibrous SACs showed distinctly better catalytic performance than the state-of-the-art SACs in various important acid-catalyzed liquid-phase reactions, including both hydrophilic and hydrophobic acid-catalyzed reactions. The superior performance of the nanofibrous SACs is associated to their unique structural feature and surface chemistry, i.e., high specific surface areas, large pore volumes, and high SO3H density and total acid density. The concept of converting nanofibrous cellulose to SACs demonstrated in this work sheds new light on the further development of highly efficient catalysts based on nanostructured biomass for green and sustainable chemistry.

4. Materials and Methods

4.1. Materials and Chemicals

Raw materials of purified BC pellicles with fiber content of ~1% (vol/vol) were kindly provided by Ms C. Y. Zhong (Hainan Yeguo Foods Co. Ltd, Hainan, China). The fuming sulfuric acid (50 wt% SO3) was purchased from Nanjing Chemical Reagent Co. Ltd (Nanjing, China). Amberlyst-15, Nafion R-1100, and niobic acid were obtained from Puzhen Biological Technology Co. Ltd., Alfa Aesar (China) Chemicals Co. Ltd., and Macklin Biochemical Co. Ltd. (Shanghai, China), respectively. H-ZSM-5 and H-Mordenite were purchased from Shengtan Environmental New Materials Co. Ltd (Shanghai, China). Other chemicals were of analytical grade, commercially available from Sinopharm Chemical Reagent Co. Ltd (Shanghai, China), and used as received without further purification.

4.2. Preparation of BC-CNFs-SH SACs

The as-received purified BC pellicles with a thickness of 1 cm were first soaked with deionized water for 3 days and cut into small pieces. Then, the small BC pieces were immersed in 10 mM NH4H2PO4 solution for 3 days and freeze-dried to obtain BC aerogels. The BC aerogels were subsequently heated to 400-800°C under a N2 atmosphere with at a heating rate of 5°C min−1 speed and kept for 2 h to generate BC-CNFs aerogels. The BC-CNFs aerogels were then sulfonated using concentrated H2SO4 at 150°C or fuming H2SO4 (50 wt% SO3) at 100°C for 12 h, respectively, before cooling to room temperature and washing with hot distilled water (>80°C) until impurities, such as sulfate ions, were no longer detected in the wash water. Finally, the sulfonated products were freeze-dried to obtain BC-CNFs-SO3H SACs. The cellulose-600-SO3H and glucose-600-SO3H as reference samples were prepared by the same processes using concentrated H2SO4 for sulfonation. Of note, the precursor of glucose-600-SO3H, i.e., glucose, has not been impregnated with deionized water and 10 mM NH4H2PO4 solution before use, due to the high solubility in water.

4.3. Characterization

SEM images were taken with a Zeiss Supra 40 scanning electron microscope at an acceleration voltage of 5 kV. TEM images were obtained using a Hitachi H7650 or Hitachi H7700 transmission electron microscope with a CCD imaging system and an accelerating voltage of 100 kV. XRD data was collected on a Philips X’Pert PRO SUPER X-ray diffractometer equipped with graphite monochromatic Cu Kα radiation (λ = 1.54056 Å). EDS spectrum and corresponding elemental mapping were acquired using a Talos F200X transmission electron microscope at an accelerating voltage of 200 kV equipped with an energy dispersive detector. FT-IR spectroscopy was measured on a Bruker Vector 22 Fourier transform infrared spectrometer. 13C MAS NMR spectra were recorded on a Bruker AVANCE 400WB NMR spectrometer (400 MHz). N2 sorption analysis was carried out using an ASAP 2020 accelerated surface area and porosimetry instrument (Micromeritics), equipped with automated surface area, at 77 K using Barrett-Emmett-Teller (BET) calculations for the surface area. The pore size distribution plot was analyzed from the adsorption branch of the isotherm based on the Barrett-Joyner-Halenda (BJH). Raman scattering spectra were recorded with a Renishaw System 2000 spectrometer using the 514.5 nm line of Ar+ for excitation. XPS was performed on an X-ray photoelectron spectrometer (ESCALab MKII) with an excitation source of Mg Kα radiation (1253.6 eV). The XAS tests of C K-edge and O K-edge were carried out at the BL11U beamline of National Synchrotron Radiation Laboratory (NSRL, Hefei, China). The S K-edge was performed at the beamline 4B7A beamline of Beijing Synchrotron Radiaition Facility (BSRF, Beijing, China). The XAS spectra in the figures have been normalized to the background before and after the main features. The GC instrument was equipped with a Restek-5 capillary column (5% diphenyl and 95% dimethylsiloxane, 0.32 mm diameter, 60 m length) and a flame ionization detector (FID). Gas chromatograph (GC, Shimadzu GC-2014) was used to calculate the conversion and selectivity of the catalytic products.

4.4. Catalytic Reactions

Dimerization of AMS was performed in a 5 mL glass reactor sealed with a Teflon lid. AMS (1 ml) was reacted over the catalyst (5 mg) at 100°C for 20 h unless otherwise specified. After cooling to room temperature, -heptadecane was added as an internal standard and then ethanol (10 ml) as a diluent was added. Samples were withdrawn at intervals from the reaction mixtures and analyzed by gas chromatography using a capillary column.

Esterification of higher fatty acids was performed in a mixture containing 0.010 mol methanol, 0.001 mol oleic acid, 1 ml n-octane mixture, and 5 mg catalyst at 80°C for 6 h. After cooling to room temperature, n-heptadecane was added as an internal standard and then n-octane (10 ml) as a diluent was added. The liquid phase was separated from the reaction mixtures and analyzed by gas chromatography using a capillary column.

Pinacol-pinacolone rearrangement was carried out in the liquid phase as follows. 5 mg catalyst, pinacol (1.0575 mol), and 1 ml water were added in glass reactor. Then they were heated to 130°C and kept for 12 h. After cooling to room temperature, n-heptadecane was added as an internal standard and toluene (10 ml) as a diluent was also added. At last, the liquid phase was analyzed using gas chromatography with capillary columns.

Catalytic synthesis of β-enamino ketones/esters was carried out in a round bottom flask. Typically, 10 mg catalyst was added into a reactant mixture of diketone (5 mmol) and amine (5.2 mmol). The reaction was performed in air atmosphere with magnetically stirring at 60°C for 0.1-3 h. The reactants and products were analyzed by gas chromatography, and the yield of all reactions refers to the GC yield.

Hydrogenation of nitrobenzene was performed in the presence of 0.3 g nitrobenzene, 0.85 mL hydrazine monohydrate, and 5 mg catalyst at 100°C for 4 h. After cooling to room temperature, 10 ml methanol (diluent) and n-dodecane (internal standard) were added, and the liquid phase was analyzed using gas chromatography with capillary columns.

Data Availability

All data needed to evaluate the conclusions in the paper are present in the paper and the Supplementary Materials. Additional data related to this paper may be requested from the authors.

Conflicts of Interest

The authors declare no financial conflicts of interest.

Authors’ Contributions

Zhen-Yu Wu and Peng Yin contributed equally to this work. Shu-Hong Yu, Hai-Wei Liang, Zhen-Yu Wu, and Peng Yin conceived and designed the experiments. Shu-Hong Yu and Hai-Wei Liang supervised the research. Peng Yin, Zhi-Qin Chen, Chao Li, and Si-Cheng Li conducted the synthesis of the catalysts. Zhen-Yu Wu and Peng Yin performed the catalyst characterizations and catalytic experiments. Huan-Xin Ju and Jun-Fa Zhu assisted with XAS measurement and data analysis. Shu-Hong Yu, Hai-Wei Liang, Zhen-Yu Wu, and Peng Yin cowrote the paper. All authors discussed the results and commented on the manuscript.


Shu-Hong Yu acknowledges the funding support from the National Natural Science Foundation of China (Grants 21431006, 21761132008), the Foundation for Innovative Research Groups of the National Natural Science Foundation of China (Grant 21521001), Key Research Program of Frontier Sciences, CAS (Grant QYZDJ-SSW-SLH036), and the Users with Excellence and Scientific Research Grant of Hefei Science Center of CAS (2015HSC-UE007). Hai-Wei Liang is thankful for the support by “the Recruitment Program of Global Experts,” National Natural Science Foundation of China (Grant 21671184), and the Fundamental Research Funds for the Central Universities (Grant WK2340000076). Zhen-Yu Wu acknowledges the funding support from the National Postdoctoral Program for Innovative Talents (Grant BX201600142), the China Postdoctoral Science Foundation (Grant 2017M610383), the Fundamental Research Funds for the Central Universities (Grant WK2060190077), and the National Natural Science Foundation of China (Grant 21703229). This work was partially carried out at the USTC Center for Micro and Nanoscale Research and Fabrication.

Supplementary Materials

Figure S1: SEM and TEM images of BC-CNFs-400. Figure S2: SEM and TEM images of BC-CNFs-600 and BC-CNFs-600-SO3H. Figure S3: SEM and TEM images of BC-CNFs-800 and BC-CNFs-800-SO3H. Figure S4: SEM and TEM images of BC-CNFs-400-SO3H∗. Figure S5: EDS spectra of BC-CNFs-400-SO3H and BC-CNFs-400-SO3H∗. Figure S6: Elemental mapping images of BC-CNFs-400-SO3H network. Figure S7: Elemental mapping images for an individual nanofiber of BC-CNFs-400-SO3H∗. Figure S8: Elemental mapping of BC-CNFs-400-SO3H∗ network. Figure S9: XRD patterns. Figure S10: Raman spectra. Figure S11: N2 adsorption-desorption isotherms and pore size distribution curves of BC-CNFs-400 and BC-CNFs-400-SO3H. Figure S12: N2 adsorption-desorption isotherms and pore size distribution curves of BC-CNFs-600-SO3H, BC-CNFs-800-SO3H, and BC-CNFs-400-SO3H∗. Figure S13: 13C MAS NMR spectra. Figure S14: The measurement of contact angles with water for BC-CNFs-400-SO3H, BC-CNFs-600-SO3H, BC-CNFs-800-SO3H, and BC-CNFs-400-SO3H∗. Figure S15: C 1s, O 1s, and S 2p high resolution XPS spectra of BC-CNFs-600, BC-CNFs-600-SO3H, BC-CNFs-800, BC-CNFs-800-SO3H, BC-CNFs-400, and BC-CNFs-400-SO3H∗. Figure S16: C K-edge, O K-edge, and S K-edge XAS spectra. Figure S17: Time courses for AMS conversion and yields of unsaturated dimers and saturated dimers. Figure S18: The dimerization of AMS over H2SO4 in the absence and presence of p-cresol (2.4 mL). Figure S19: AMS dimerization performance comparison among glucose-600-SO3H, cellulose-600-SO3H, and BC-CNFs-600-SO3H. Figure S20: Recyclability performance of BC-CNFs-600-SO3H for AMS dimerization. Figure S21: TEM images of recycled BC-CNFs-600-SO3H after catalyzing AMS dimerization for four times. Figure S22: Recyclability performance of BC-CNFs-400-SO3H for esterification of oleic acid with methanol. Figure S23: Recyclability performance of BC-CNFs-400-SO3H for pinacol rearrangement. Figure S24: 31P MAS NMR spectra of BC-CNFs-400-SO3H∗ and some reference SACs. Figure S25: Recyclability performance of BC-CNFs-400-SO3H for hydrogenation of nitrobenzene. Figure S26: Characterizations for Wood-CNFs-400-SO3H. Figure S27: Characterizations for phosphorylated BC-CNFs-400. Table S1: Catalytic performance of the catalysts tested for synthesis of β-Ketoenamines. Table S2: The comparison of catalytic performance of BC-CNF-400-SO3H and previously reported carbon-based catalysts for hydrogenation of nitrobenzene. References [9, 18, 43, 44]. (Supplementary Materials)


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