Ping-Chang
Chuang
and
Yi-Hsuan
Lai
*
Department of Materials Science and Engineering, National Cheng Kung University, No.1, University Road, Tainan City 701, Taiwan. E-mail: yhlai@gs.ncku.edu.tw
First published on 21st July 2022
Electrochemical and photoelectrochemical valorisation of biomass is an attractive technology to provide value-added chemicals such as formate in a sustainable way. Monoclinic CuO acting as an efficient non-precious electrocatalyst for formate production from glucose and cellulose is reported. Notably, a high faradaic efficiency of 94.1 ± 1.5% and a turnover frequency of 240.2 ± 16.3 h−1 for formate production at an applied potential of 1.5 V vs. reversible hydrogen electrode (RHE) are achieved using monoclinic CuO as the electrocatalyst for glucose oxidation. The mechanism of formate generation from electrocatalytic oxidation of glucose is elucidated by product analyses and electron paramagnetic resonance (EPR) study. The results suggest that one glucose is oxidised to one formate and one pentose mediated by the generation of OH radicals during the electrolysis. Electrocatalytic formate production using purified α-cellulose and “real world” biomass wastes was also investigated. In particular, a moderate faradaic efficiency of 41.4 ± 9.7% was observed using rice straw as the substrate. Furthermore, monoclinic CuO acts as an efficient cocatalyst on a hematite photoanode, showing a faradaic efficiency of 97.3 ± 2.8% for formate production through photoelectrochemical glucose valorisation.
Traditional methods for producing formic acid from biomass include pyrolysis,4 wet oxidation,5 catalytic oxidation,6 and acid hydrolysis.7 Although high yields of formic acid can be produced using these conventional methods, several inherent disadvantages are also present. For example, a high temperature (450–650 °C) is generally required in pyrolysis to obtain high yields of formic acid.4 On the other hand, additional oxidants and high-pressure O2 (1–5 Mpa) are typically needed for wet and catalytic oxidation processes, respectively.5,8 In contrast, electrochemical oxidation is an emerging methodology in biomass valorisation. Electrochemical oxidation eliminates the need for hazard oxidants and is generally operated under ambient or mild conditions. The product selectivity is possibly tuned by the applied potentials.2,9 In addition, hydrogen and value-added chemicals can be co-produced through hydrogen evolution and biomass oxidation at the cathode and anode, respectively, in an electrochemical system.2,10 Last but not least, since biomass oxidation is less energy demanding than water oxidation, the efficiency of converting solar light into storable chemical energy in a photoelectrochemical (PEC) biomass cell is expected to be higher than that of a PEC water splitting cell.11
Several noble metals and alloys, such as Au,9,12 Pt,9 and PdAu,13 have been investigated as efficient electrocatalysts for converting glucose to gluconic acid and glucaric acid by the oxidation aldehyde group on C1 and the hydroxymethyl group on C6, respectively (Table S1†). However, it is essential to explore other selective and efficient electrocatalysts made of inexpensive and earth-abundant elements if (photo)electrochemical biomass valorisation is to be a viable technology. For glucose valorisation, rare examples of earth-abundant electrocatalysts, including NiFeOx,2 Cu,9 and CuBi2O4,14 have been recently reported. It is found that only Cu-based materials can effectively catalyse C–C bond breaking, resulting in the formation of formate. However, mixtures of low molar mass carboxylic acids, gluconic acid, and glucaric acid are co-present in the products.9 The low selectivity of formate might result from the complex surface states on Cu. In particular, it is known that Cu2O, CuO, and Cu(OH)2 are co-present on the surface of Cu under anodic potentials higher than 1.0 V in alkaline solutions.15
On the other hand, CuO is relatively stable compared to Cu under anodic conditions.15a CuO has also been widely used as an electrochemical sensor for glucose detection.16 The limited reports on CuO acting as a selective electrocatalyst for biomass valorisation include glycerol oxidation to dihydroxyacetone.17 However, to the best of our knowledge, there is no report on a pure phase of CuO acting as a highly selective electrocatalyst for formate production from glucose, along with detailed product analyses and mechanism discussion.
In this work, we synthesised a monoclinic CuO thin film on a fluorine-dope tin oxide (FTO) electrode. CuO shows high selectivity in terms of faradaic efficiency for formate production (FEformate) from glucose in alkaline solutions. Formate also can be electro-catalytically generated at CuO by using cellulose, a homopolymer of glucose, as the substrate with a moderate FEformate. We also demonstrate that formate production is also applicable to the electrooxidation of crude sources of cellulose, including tissue paper and rice straw. Last but not least, for the first time, CuO was decorated onto a hematite (α-Fe2O3) photoanode for selective PEC glucose valorisation. This composite photoelectrode made of only earth-abundant materials performs photoelectrochemical valorisation with a FEformate of approximately one unit.
The electrooxidation performance of m-CuO was first evaluated in 0.1 M NaOH with various concentrations of glucose. Without the addition of glucose, no noticeable electrocatalytic current is observed until the potential is more positive than 1.7 V vs. reversible hydrogen electrode (RHE), which is assigned to water oxidation reaction (Fig. S4†). In contrast, in the presence of glucose, oxidative currents increase dramatically with an onset potential of approximately 1.2 V vs. RHE in the cyclic voltammograms (CVs). The oxidative currents increase with an increment of glucose concentration and reach the saturated catalytic current at a glucose concentration of 20 mM. Further enhancement in the glucose concentration does not result in further enhancement in the catalytic current, and this might be attributed to the limited active sites on m-CuO for glucose oxidation.
The prepared m-CuO was subsequently subjected to the 1 h controlled potential electrolysis (CPE) in a NaOH (0.1 M) containing 20 mM glucose at potentials of 1.3 V, 1.4 V, 1.5 V, and 1.6 V vs. RHE (Fig. 2b). The generation rate and electrocatalytic index, including the turnover frequency of formate (TOFformate) and FEformate, are shown in Fig. 2c. High-performance liquid chromatography (HPLC) analyses were performed for formate quantification (see Experimental for details). We are aware that a trace amount of formate was possibly generated by a self-degradation of glucose during the prolonged electrolysis in an alkaline solution (Table S2†). For accurate quantification of FEformate and TOFformate, the amount of formate produced by the chemical reaction was excluded from the total amount of formate (see Table S2† and Experimental for details). The results indicate that formate can be generated by electrocatalytic oxidation using m-CuO at potentials higher than 1.3 V vs. RHE with a formate production rate (Rformate) rate of 2.00 ± 0.49 μmol h−1 cm−2. Rformate dramatically increased to 154.73 ± 10.53 μmol h−1 cm−2 and 175.62 ± 5.97 μmol h−1 cm−2 at 1.5 V and 1.6 V vs. RHE, respectively. The TOFformate value of m-CuO is estimated by dividing Rformate (μmol h−1 cm−2) by the amount of the catalyst (μmol cm−2) and the duration of CPE (h). Cu was found to be 0.64 μmol cm−2 by inductively coupled plasma (ICP) measurements (see Experimental for details). The TOFformate of m-CuO is highly dependent on the applied potential, ranging from approximately 3.1 to 272.6 h−1 between 1.3 and 1.6 V vs. RHE (Fig. 2c). On the other hand, m-CuO shows a similarly high FEformate (>80%) in the potential window between 1.3 and 1.6 V vs. RHE and reaches the highest FEformate value of 94.1 ± 1.5% at 1.5 V. The slight decrease of FEformate at an applied potential >1.5 V is possibly attributed to water oxidation to oxygen or the further electrochemical oxidation of formate.
To monitor the dynamic performance of m-CuO toward electrocatalytic glucose valorisation, HPLC analyses were performed at different charge quantities(Fig. 2d and S5†). The corresponding FEformate is summarised in Fig. S6,† and the results indicate that formate is selectively generated with over 90% FEformate in the entire electrolysis. Except for formate, significant amounts of fructose and pentose (xylose and arabinose), as well as a trace amount of lactate, were found (Fig. 2d). It is known that fructose can be generated from the isomerisation of glucose in an alkaline solution.19 Other typical glucose oxidation products, such as glucaric acid and gluconic acid, were not observed (Fig. S5†). It is worth noting that the amount of formate and pentose continuously increased with the passed charge, while glucose was constantly consumed. After the charge of 40 C was passed, approximately 194 μmol of formate and 158 μmol of pentose (xylose and arabinose) were generated, while approximately 188 μmol of glucose was consumed. However, only 158 μmol of glucose was consumed by electrolysis since approximately 30 μmol of glucose was isomerised to fructose. The molar ratio of formate and pentose generation to glucose consumption by electrolysis is 1.2:1:1 (formate:pentose:glucose), suggesting that one glucose might be electro-oxidised to one formate and one pentose. The slight deviation from the 1:1 ratio of formate generation and glucose consumption possibly resulted from that extra amount of formate produced by the chemical and electrochemical degradation of C2–C5 during the electrolysis.
For comparison, electrocatalytic glucose oxidation has also been performed with Cu foil and pre-oxidised Cu foil. Pre-oxidised Cu foil was prepared by electro-oxidising Cu foil in an alkaline solution. An oxidation peak of Cu foil is observed at approximately 1.03 V in the CV (Fig. S7†). Therefore, Cu foil was subjected to oxidising at 1.03 V in 0.5 M KOH solution for 1 h to obtain the pre-oxidised Cu foil. The XPS core-level spectrum of Cu 2p confirms that the surface of pre-oxidised Cu foil is composed of a mixture of Cu, CuO, and Cu(OH)2 (Fig. S8a†), although the main composition is still Cu. Furthermore, the XPS core-level spectrum of O 1s also supports the existence of CuO and Cu(OH)2 on Cu foil after the pre-oxidised treatment (Fig. S8b†). The catalysts showed a decreased electrocatalytic activity toward formate production from electro-oxidising glucose in the sequence of m-CuO, pre-oxidised Cu foil, and Cu foil (Table S3†) in terms of Rformate. In particular, Cu foil has a Rformate of 76.03 μmol cm−2 h−1, approximately only half of that generated using m-CuO. Although the pre-oxidised Cu foil has a comparable Rformate with m-CuO, it has a lower FEformate of 82.0% compared to m-CuO (94.1%). Since the sequence (Cu foil < pre-oxidised Cu foil < m-CuO) of electroactivity toward the formate production from glucose is consistent with the sequence of contents of CuO, CuO is most likely the active material toward C–C breaking.
There is a controversy about the mechanism of glucose oxidation by CuO. It has been previously accepted that Cu3+ plays the dominant role in glucose oxidation, in which Cu3+ is firstly formed by the oxidation of Cu2+ under anodic potential followed by directly oxidising glucose.20 However, Cu3+ species are only formed at a highly anodic potential where water oxidation occurs.21 The CV results indicate that m-CuO catalyse water oxidation along with the formation of Cu3+ at approximately 1.7 V vs. RHE in 0.1 M NaOH, while a reduction peak assigned to the reduction of Cu3+ is observed approximately at 1.65 V vs. RHE (Fig. S4†). However, m-CuO can perform electrochemical oxidation of glucose to formate at potentials of 1.3 to 1.6 V vs. RHE, below the potential of Cu3+ formation. The results suggest that other mechanisms mediated the reaction at m-CuO from 1.3 to 1.6 V vs. RHE.
Hydroxyl (OH) radical-mediated glucose oxidation has been recently proposed.16,21b,22 CuO is a p-type semiconductor,23 and the p-type feature of m-CuO can be confirmed by the negative slope in the Mott–Schottky analysis (Fig. S9†). For a p-type material, vacancies accumulate in the interface region when the applied potential is more positive than its flat band potential (VFB).24 It is believed that when the applied potential is more positive than the VFB of CuO, the absorbed OH ions can be oxidised by the accumulation of vacancies in the interface region of CuO followed by the generation of OH radicals.21b The OH radicals, acting as strong oxidants, subsequently react with glucose. In order to elucidate the mechanism of m-CuO electrocatalytic glucose oxidation, EPR analyses were performed by using 5,5-dimethyl-1-pyrroline-N-oxide (DMPO) as the trapping agent of OH radicals. The VFB of m-CuO is approximately 1.15 V vs. RHE, as determined by Mott–Schottky analyses (Fig. S9†). The EPR spectrum shows CuO in 1 M NaOH solution after 10 min electrolysis at 1.5 V (Fig. 3a), revealing a well-defined four-line pattern with an intensity ratio of 1:2:2:1 and hyperfine splitting of αN = αH = 15 G, corresponding to the characteristic of a DMPO–OH adduct,25 which confirms the presence of OH radicals.
It should be noted that, however, prior to electrolysis, the signals for the DMPO–OH adduct were present (Fig. S10†). However, no significant difference in the intensity of signals between the background signal and electrolysis at the OCP or 1.2 V vs. RHE, indicating that potentials before or near VFB of m-CuO do not result in the formation of further OH radical by electrolysis. However, m-CuO exhibited significantly higher intensity at potentials of 1.5 V vs. RHE, indicating that electrolysis at a potential more positive than the VFB of m-CuO generated more OH radicals. The OH radicals were subsequently consumed by glucose, which was supported by the signals of the DMPO–OH adduct completely disappeared in the presence of glucose (Fig. 3b).
The mechanism of formate production from glucose oxidation at m-CuO is therefore proposed based on the electrochemical study, product analyses, and the EPR spectra. At the potentials between 1.3–1.6 V vs. RHE, where the potentials are higher than the VFB of m-CuO, OH radicals are formed by the absorbed OH ions with the accumulated vacancies at the m-CuO surface. Subsequently, two OH radicals react with one glucose to generate one formate and one pentose (Fig. 3c).
Since m-CuO acts as a selective electrocatalyst for formate production from glucose, we were interested in determining if formate can be efficiently electrochemically produced at m-CuO by using α-cellulose, a homopolymer of glucose, which is also the most abundant form of forest biomass as the substrate. However, α-cellulose has very low solubility in solutions. Therefore, a pretreatment process involving stringing the α-cellulose in a strongly alkaline solution was applied before the electrochemical study (see Experimental for details). Trace amounts of glucose of approximately 0.038 mM were found in the pretreated α-cellulose solution. An onset oxidation potential at 1.2 V vs. RHE and an oxidation wave centred at 1.58 V vs. RHE followed by water oxidation at 1.7 V vs. RHE are observed in the presence of cellulose (Fig. 4a). On the other hand, no noticeable oxidation current is observed without α-cellulose at potentials of 1.2–1.7 V vs. RHE. However, a reduction wave centred at 1.65 V vs. RHE can be observed in both solutions with and without cellulose. The reduction wave can be attributed to the reduction of Cu3+ to Cu2+, whereas the oxidation wave of Cu2+ to Cu3+ overlapped with water oxidation.26 The electrochemical results suggest that cellulose and its derivatives can be oxidised at potentials more positive than 1.2 V vs. RHE. In addition, the CV curves of m-CuO negatively shifted with the increase of the pH value with a rate of 0.059 × pH, suggesting that hydroxide ions followed by the formation of OH radicals participate in α-cellulose oxidation at potentials before water oxidation. The electrochemical features are similar to those of glucose oxidation at m-CuO, and presumably, glucose oxidation contributed to at least a partial oxidation current.27
Subsequently, experiments of m-CuO electrocatalysing α-cellulose oxidation at various potentials were performed. m-CuO shows moderate catalytic activity towards reforming α-cellulose to formate, and the FEformate increase from 14.3 ± 5.3% to 29.7 ± 4.2% at 1.3 V vs. RHE and 1.5 V vs. RHE, respectively. Although m-CuO generated a higher current at 1.6 V than 1.5 V (Fig. 4c and S11†), the TOFformate value was similar to that at 1.5 V (0.39 h−1vs. 0.38 h−1). Additionally, the FEformate value dramatically decreases at potentials higher than 1.5 V vs. RHE, presumably due to the side reaction of water oxidation starting at 1.6 V vs. RHE. Replacement of purified α-cellulose with raw “real-world” biomass waste results in even high FEformate by using m-CuO as the electrocatalyst. FEformate values of 34.1 ± 3.3% and 41.4 ± 9.7% were quantified by using tissue paper and rice straw as the substrate, respectively, from 2.5 h CPE at 1.5 V vs. RHE. In particular, rice straw has over 2.5-fold Rformate compared to purified α-cellulose from 2.5 h CPE at 1.5 V (Table S4†).
m-CuO was subsequently coated on a hematite (α-Fe2O3) electrode to demonstrate that m-CuO can be used as a cocatalyst on a photoanode to perform selective photoelectrochemical glucose valorisation. Hematite is robust in alkaline solutions. It has been immensely investigated as a photoanode for solar-driven water oxidation due to its narrow bandgap and proper electronic band structure, capable of using visible light to drive water oxidation. However, hematite shows low selectivity toward organic compounds oxidation such as glycerol.28
Nanorod structure hematite (nanoFe2O3) was converted by heating the substrate of β-FeOOH at 800 °C for 20 min. β-FeOOH was synthesised by a chemical bath deposition method (see Experimental for details and Fig. S12†). To prepare m-CuO modified nanoFe2O3 (nanoFe2O3|m-CuO), one layer of the copper precursor was spun onto nanoFe2O3, followed by the same heat treatment process used for preparing m-CuO (Fig. 5a). The cherry red colour of nanoFe2O3 became wine red colour after m-CuO modification (insets of Fig. 5b and c). GI-XRD confirms that the nanoFe2O3 is consistent with the phase of α-Fe2O3 (JCPDS No. 33-0664). Additional peaks at 2 theta of 32.50 and 38.80 are observed in nanoFe2O3|m-CuO, which belong to the (110) and (111) planes of the monoclinic phase of CuO (JCPDS 48-1548), respectively. The SEM images indicate that nanoFe2O3 has a rod-like structure with a rod diameter and length of approximately 60 nm and 0.4 μm, respectively, similar to its FeOOH template (Fig. 5b, b′ and S12†). On the other hand, nanoFe2O3|m-CuO remains to be the rod structure of nanoFe2O3, although its rod diameter increases to 90–200 nm (Fig. 5c, c′).
The electronic structure of nanoFe2O3 and m-CuO can be estimated from their UV-vis spectra and Mott–Schottky analyses. The direct bandgap of m-CuO and nanoFe2O3 is 1.7 eV and 2.15 eV, respectively, consistent with the reported values (Fig. S13 and S14†).23a,29 The positive slope in the Mott–Schottky analysis plot of nanoFe2O3 confirms its n-type feature, and its flat band edge is estimated at 0.35 V vs. RHE from the extrapolated intercepts. For an n-type semiconductor, its conduction band is close to its flat band edge. Therefore, the valence band edge of nanoFe2O3 can be estimated from its bandgap and conduction band edge and is approximately 2.5 V vs. RHE (Fig. 6a). The water and glucose oxidation potentials are 1.23 V vs. RHE and 0 V, respectively.30 Under solar light illumination, the holes of nanoFe2O3 can provide sufficient driving force for both water oxidation and glucose oxidation. However, the sluggish water oxidation kinetics of nanoFe2O3 resulted in its onset potential of 0.7 V vs. RHE, significantly deviating from its flat band edge of 0.35 V vs. RHE (Fig. 6c(i)). In the presence of glucose, the onset potential negatively shifts to 0.5 V vs. RHE, and the photocurrents increased more than two times at 1.23 V vs. RHE, which indicates that the glucose oxidation kinetics is more facile than water oxidation. Nevertheless, since nanoFe2O3 catalyses both water and glucose oxidation under light illumination, it shows only a moderate FEFormate of approximately 60.8 ± 1.5% toward glucose oxidation at 1.0 V vs. RHE (Fig. 6f).
The unsatisfactory selectivity of formate production from glucose oxidation on nanoFe2O3 is possibly alleviated by passivating it with m-CuO. Firstly, m-CuO can serve as an efficient electrocatalyst on nanoFe2O3. Secondly, the oxidative force of the light-induced holes is possibly tuned by the n–p heterojunction of nanoFe2O3 and m-CuO (Fig. 6b). The valence band edge of m-CuO is located near its flat band potential of 1.15 eV. Therefore, the light-induced holes of the heterostructure of nanoFe2O3|m-CuO are only able to oxidise glucose. This hypothesis can be evident from the current density-potential curves under chopped light illumination. The nanoFe2O3 photoelectrochemical water oxidation was almost eliminated by passivating m-CuO (Fig. 6d(i)). In addition, the photocurrent of nanoFe2O3|m-CuO in NaOH solution containing glucose is 15 times higher than that without glucose at potentials 1.23 V vs. RHE. NanoFe2O3|m-CuO exhibited stable photocurrent and a high FEformate of 97.3 ± 2.8% in NaOH solution containing 20 mM glucose at 1.0 V vs. RHE (Fig. 6e and f). This serves as a rare example of using only earth-abundant materials for the highly selective photoelectrochemical valorisation of organic compounds to formate (Table S5†).
NanoFe2O3 was synthesised by a chemical bath deposition method followed by a heat-treatment process. Briefly, FTO glass was immersed into a bottle containing 0.15 M FeCl3·H2O (Sigma Aldrich, 99%) and 1 M NaNO3 (J.T. Baker, 99%) aqueous solution. The bottle was then sealed and heated at 100 °C for 6 h. The resultant bright yellow β-FeOOH nanorod electrode was subsequently converted to nanoFe2O3 in a preheated tube furnace by annealing at 800 °C for 20 min. NanoFe2O3|m-CuO was synthesised by spin-coating one layer of the CuO precursor, and the heat treatments were the same as that for the preparation of the m-CuO electrode.
The FEformate and TOFformate are calculated using the following equations (eqn (1) and (2)):
(1) |
(2) |
For reforming α-cellulose, tissue paper and rice straw, formate was detected by 883 Basic IC plus ion chromatography (Metrohm) equipped with a Metrosep organic acids guard (4.6 × 50 mm) and a Metrosep organic acids column (7.8 × 250 mm) rather than HPLC to avoid the interference from carbohydrate signals.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d2cy00950a |
This journal is © The Royal Society of Chemistry 2022 |