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Unassisted solar lignin valorisation using a compartmented photo-electro-biochemical cell

Abstract

Lignin is a major component of lignocellulosic biomass. Although it is highly recalcitrant to break down, it is a very abundant natural source of valuable aromatic carbons. Thus, the effective valorisation of lignin is crucial for realising a sustainable biorefinery chain. Here, we report a compartmented photo-electro-biochemical system for unassisted, selective, and stable lignin valorisation, in which a TiO2 photocatalyst, an atomically dispersed Co-based electrocatalyst, and a biocatalyst (lignin peroxidase isozyme H8, horseradish peroxidase) are integrated, such that each system is separated using Nafion and cellulose membranes. This cell design enables lignin valorisation upon irradiation with sunlight without the need for any additional bias or sacrificial agent and allows the protection of the biocatalyst from enzyme-damaging elements, such as reactive radicals, gas bubbles, and light. The photo-electro-biochemical system is able to catalyse lignin depolymerisation with a 98.7% selectivity and polymerisation with a 73.3% yield using coniferyl alcohol, a lignin monomer.

Introduction

Biomass is considered a promising replacement for fossil fuels because it is the most abundant carbon source in nature and is carbon neutral1,2. There has been remarkable progress on biomass conversion technologies, especially the conversion of sugar or starch crops to biofuels and various chemicals. However, the use of edible biomass as a feedstock is controversial in terms of ethics and cost3. Hence, waste biomass, so-called lignocellulosic biomass, such as wood residues, straw, and crop stover, have recently emerged as promising carbon sources3.

Lignin is one of the three major components of lignocellulosic biomass, together with cellulose and hemicellulose. It is nature’s most abundant source of aromatic carbon compounds and can be potentially transformed into high-value products4,5,6,7,8,9,10,11. However, because of its complex/irregular chemical structure and currently limited processing technology, more than 99% of lignin is abandoned or burned12. To make lignocellulosic biomass a more compatible renewable carbon source, an effective method for lignin valorisation is vital. The key issue here is finding effective strategies for the selective cleavage of carbon–oxygen bonds (C–O–C), more specifically, the β-ether (β-O-4) bond connecting the three basic aromatic units (coumaryl alcohol, coniferyl alcohol, and sinapyl alcohol); this is a critical step for the depolymerisation of lignin to yield valuable aromatic chemicals and feedstocks13,14,15,16,17.

Various treatment technologies including physical (ball milling, ultrasonication, plasma irradiation, and microwave heating), chemical (using an organic or inorganic acid), or catalytic (with a heterogeneous catalyst) methods have been used for lignin valorisation18,19,20,21. However, these processes are usually energy-intensive, requiring high temperatures and pressures, and environmentally unfriendly, producing chemical waste. Most importantly, selective carbon–oxygen bond breakage is not plausible using these conventional methods. However, microorganisms including fungi and bacteria have been selectively degrading lignin for more than 300 million years, although the detailed mechanism remains elusive22. In particular, the lignin peroxidase isozyme H8 (LiPH8) biocatalyst from white rot fungi has received much attention because of its exceptional ability for the selective cleavage of β-O-4 bonds in lignin23,24,25. However, a critical limitation of biocatalyst systems is that hydrogen peroxide (H2O2), which acts as an electron acceptor, must be provided from an external source, and its high concentration is detrimental to enzyme stability, limiting the scale-up of these systems.

The integration of the H2O2 generation system with the biocatalytic conversion system allows for continuous production and utilisation of H2O2, which would allow the use of low concentrations of H2O2 and the production of large-scale devices. The current method of producing H2O2 is predominantly based on the anthraquinone process, which consists of multi-step processes and requires additional separation steps in the presence of high pressure H2 and expensive precious metal catalysts26. Direct reaction of H2 and O2 on a catalyst is a simple and clean process, but this requires high-pressure gases (H2 and O2)27,28. Therefore, the anthraquinone process and direct H2O2 synthesis are not compatible with biocatalytic systems. In contrast, electrochemical H2O2 production via two-electron O2 reduction is a simple, clean, safe, and low-cost process29,30,31. Furthermore, this process operates under ambient pressure and temperatures, enabling its facile integration with the biocatalytic system. However, a critical limitation remains: additional electrical energy must be supplied to operate this integrated system.

On the other hand, photocatalysis can also produce H2O2 in a straightforward, clean manner and can be operated under ambient conditions like electrocatalytic H2O2 production. On the irradiation of the photocatalyst with light, excited electrons are produced in the conduction band, and these are then utilised for O2 reduction, producing H2O2. Recently, several groups have combined this photocatalytic H2O2 system with biocatalysts and applied them for various chemical reactions. For example, a modified powder-type TiO2 photocatalyst was utilised for H2O2 generation, and it was integrated with a biocatalytic system of peroxygenases for the selective oxyfunctionalisations of carbon–hydrogen bonds, which has been one of the major challenges in organic synthesis32,33,34,35. However, this integrated system (biocatalytic system with photocatalytically generated H2O2) has been rarely applied for lignin valorisation, and most of the research has been focused on developing an efficient powder-type photocatalyst, such as Nb2O5/TiO2 heterojunction, metal-doped TiO2 or graphene–TiO2 nanocomposite for direct lignin conversion rather than for H2O2 production12,36. One of the important limitations of the integrated system is that, for efficient H2O2 generation using powder-type photocatalysts, additional chemicals are required to scavenge the remaining hole in the valence band. Most crucially, the reactive oxygen species (ROS) generated during the photochemical reaction not only destabilise the biocatalyst but also cause the random cracking/breaking of the lignin structure, thus decreasing the selectivity of lignin conversion dramatically.

Here, we propose a compartmented photo-electro-biochemical cell, in which three catalytic systems (a photocatalyst for photovoltage generation, an electrocatalyst for H2O2 production, and a biocatalyst for lignin valorisation) are integrated for selective lignin valorisation without the need for electrical energy or additional chemicals (Fig. 1). Importantly, the compartmentalisation of the three catalytic systems using Nafion and cellulose membranes stabilises the biocatalyst from enzyme-damaging elements, such as ROS, the high concentration of H2O2, shear stress from gas (O2) bubbles, and light. Moreover, because the lignin and photocatalyst are separated from each other, the dark-coloured native lignin does not reduce the light adsorption efficiency of the photocatalyst, a problem that has plagued the use of a photocatalyst for lignin valorisation (Fig. 1). The compartmented photo-electro-biochemical cell can catalyse the depolymerisation of lignin dimer with high selectivity (>95%) and the polymerisation of a benchmark lignin monomer, coniferyl alcohol, in 73.3% yield. The catalytic performance of the three-compartment system is superior to those of single-compartment and two-compartment catalytic systems.

Results

Design of the photo-electro-biochemical system

The designed photo-electro-biochemical system is composed of three compartments (photocatalyst anode, electrocatalyst cathode, and biocatalyst part), as shown in Fig. 1. Each cell is filled with an appropriate solution, and the cells are separated by Nafion and cellulose membranes. In the first compartment, a semiconductor photocatalyst receives the solar energy, and photoexcitation generates charge carriers. The photogenerated hole in the valence band oxidises water to O2, and the electrons move to the second compartment, where the electrocatalyst selectively reduces O2 to H2O2. The produced H2O2 is transferred through the size-selective cellulose membrane to the third compartment, where lignin valorisation via the biocatalyst occurs with the aid of the permeated H2O2. Importantly, the two membranes between each catalytic system prevent the permeation of O2 bubbles and ROS, such as hydroxyl radicals (•OH) and superoxide anions (•O2−), thus protecting the biocatalyst. In addition, the compartmented design ensures that the biocatalyst is not exposed to a high concentration of H2O2 and intense light because of the gradual permeation of H2O2 through the cellulose membrane and the protection of incident light by a back cover of the photoelectrode (Supplementary Fig. 1a, b), respectively. These features of the photo-electro-biochemical process allow for a continuous and stable lignin valorisation (Fig. 1).

Unassisted photo-electrochemical H2O2 production

As a photoanode for water oxidation, a rutile TiO2 nanowire film was used. This film was hydrothermally grown on a fluorine-doped tin oxide (FTO) glass substrate37 and was subsequently annealed in a hydrogen atmosphere to improve the charge transfer properties of TiO2 (denoted H:TiO2)38. The X-ray diffraction (XRD) pattern of H:TiO2 (Supplementary Fig. 2a) shows two diffraction peaks at 36.1° and 62.8°, which is consistent with that of rutile TiO2. There was no significant change in the UV–vis spectra of the TiO2 films upon hydrogen treatment (Supplementary Fig. 2b). The scanning electron microscopy (SEM) image of H:TiO2 (Supplementary Fig. 3) reveals that a homogeneous film was formed on the FTO substrate, consisting of vertically aligned nanowire arrays of 100–200 nm in diameter. Phosphate borate solution at pH 4.5 was utilised as an electrolyte. Under sunlight illumination, the photocurrent density of the bare TiO2 nanowire photoanode at 1.23 V (vs. reversible hydrogen electrode, RHE) was 0.97 mA cm−2, which is far higher than that of planar-type TiO2 electrode (0.11 mA cm−2) because of the improved charge transfer rate and increased surface area due to the nanowire morphology (Supplementary Fig. 4a). Upon hydrogen treatment of TiO2 (H:TiO2), the photocurrent density was further increased to 1.25 mA cm−2 with almost the same onset potential of 0.40 V (vs. RHE) and there was no sign of a decrease in its performance for 12 h (Fig. 2a and Supplementary Fig. 4).

The photovoltage generated at the anode is used to catalyse O2 reduction at the cathode, completing the unassisted production of H2O2. As H2O2 production electrocatalysts, cobalt porphyrins have shown high activity and selectivity for the two-electron oxygen reduction reaction (ORR)39,40. However, these molecular catalysts are incompatible with photocatalysis cells because of their instability41. In order to endow catalytic stability while preserving the intrinsic activity of the Co-porphyrin-based molecular catalysts, we used a silica-protective-layer-assisted synthesis42,43 (see the “Methods” section for detail). In the resulting catalyst, atomically dispersed Co–Nx sites are homogeneously generated on carbon nanotubes (denoted Co–N/CNT) without the aggregation of the Co species (Supplementary Fig. 5a, b). For comparison, a cobalt porphyrin molecular catalyst immobilised on the CNTs was also prepared (CoTMPP/CNT). The Co–N/CNT catalyst was found to contain 0.8 and 1.3 wt% of Co and N, respectively, as determined by inductively coupled plasma optical emission spectrometry and combustion elemental analysis, respectively. Co 2p and N 1s X-ray photoelectron spectroscopy (XPS) scans (Supplementary Fig. 6) suggest the presence of oxidised Co species (satellite peaks) and four types of N species on the surface of the Co–N/CNT catalyst. Extended X-ray absorption fine structure analysis (Supplementary Fig. 7) reveals that the Co–N coordination bonds (Co–Nx sites) of the cobalt porphyrin precursor were retained in the Co–N/CNT catalyst after the high-temperature treatment, and there is no observable Co–Co bond peak, indicating that the aggregation of Co metal was minimised by the silica-protective-layer strategy.

The ORR activity and selectivity of the Co–N/CNT and CoTMPP/CNT catalysts were investigated using the rotating ring disk electrode (RRDE) technique (Fig. 2b and Supplementary Fig. 8). The ORR polarisation curve shows that the Co–N/CNT catalyst started to generate the H2O2 production current from 0.78 V (vs. RHE) in phosphate borate solution at pH 4.5 (Fig. 2b). This onset potential is very close to thermodynamic equilibrium potential for two-electron ORR with an overpotential of only 0.04 V (Supplementary Note 1), indicating the excellent catalytic activity of the Co–N/CNT catalyst. In contrast, CoTMPP/CNT and pristine CNT required much larger overpotentials of 0.33 and 0.47 V (Fig. 2b), respectively, suggesting that the heat-treated Co–Nx structure results in high activity. RRDE and Koutecky–Levich analyses show the consistently high H2O2 selectivity (48–62%) of the Co–N/CNT catalyst (Supplementary Fig. 8b). The molecular CoTMPP/CNT catalyst shows a better H2O2 selectivity of 60–64% than Co–N/CNT, which is attributed to its well-defined Co–N4 structure. However, after being subjected to prolonged potential cycling tests, CoTMPP/CNT showed a decline in the activity for H2O2 production of around 20%, whereas the Co–N/CNT catalyst mostly maintained its activity (Fig. 2b). Scanning transmission electron microscopy (STEM) images of Co–N/CNT before and after the stability test were nearly the same, indicating that atomically dispersed Co species are not agglomerated or detached from CNT support (Supplementary Fig. 5). The Co–N/CNT catalyst is also active for electrochemical H2O2 production at low pH (in 0.1 M HClO4), extending the potential applicability of this catalyst to photocatalytic H2O2 production, as well as use with other photoanodes and biocatalysts (Supplementary Fig. 9).

Next, a large-area cathode composed of the Co–N/CNT catalyst was prepared on a piece of carbon paper for photo-electrocatalytic H2O2 production. The photo-electrocatalytic activities of the photoanode and cathode for water oxidation and the ORR, respectively, were tested in phosphate borate solution using linear sweep voltammetry (LSV) measurements. The operating current of the integrated photo-electrochemical cell could be estimated from the intersection of the LSV curves of the H:TiO2 photoanode and Co–N/CNT cathode (Fig. 2c). The intersection point in the LSV of H:TiO2 and Co–N/CNT was 0.62 mA, which far exceeds that of H:TiO2 and CoTMPP/CNT (0.09 mA), as well as those of H:TiO2 and pristine CNT (0.07 mA), highlighting the importance of an effective electrocatalyst for unassisted H2O2 production (Fig. 2c and Supplementary Fig. 10). To verify the stability of our integrated photo-electrochemical H2O2 production system, the amount of H2O2 generated on the Co–N/CNT cathode was estimated as a function of time using a colorimetric method with N,N-diethyl-p-phenylenediamine (DPD) (Fig. 2d). We observed continuous production of H2O2 over 6 h of reaction, and found that the H2O2 production rate can be easily increased by scaling up the size of electrodes and the reactor (Supplementary Fig. 11). In addition, the H2O2 produced at the cathode freely diffused into the biocatalyst cell through the cellulose membrane (Supplementary Fig. 12), enabling the utilisation of H2O2 by the biocatalyst for lignin depolymerisation and biopolymer synthesis.

Photo-electro-biochemical lignin dimer depolymerisation

There are many reported lignin model compounds, such as ferulic acid, vanillyl alcohol isoeugenol, and benzyl alcohol12,44. We selected lignin dimer as a representative model compound to observe the specific cleavage of β-O-4. For the selective cleavage of the lignin dimer into 3,4-dimethoxybenzaldehyde (a derivative of vanillin), the LiPH8 biocatalyst was used, along with the photo-electrochemically generated H2O2 (Supplementary Fig. 13). Because our three-compartment cell design protects the biocatalyst from deactivation, the enzyme activity was maintained throughout the reaction (Fig. 3a and Supplementary Fig. 14). The depolymerisation conversion efficiency and selectivity for the lignin dimer were 93.7% and 98.7%, respectively, in the three-compartment photo-electro-biochemical system (Fig. 3b, c). A control reaction carried out in the absence of the LiPH8 enzyme in the three-compartment cell indicated low conversion and selectivity, suggesting that the biocatalyst is essential for selective lignin valorisation (Supplementary Fig. 15).

For comparison, we also tested lignin depolymerisation in single-compartment and two-compartment systems. In the single-compartment system, the powder-type TiO2 photocatalyst, the LiPH8 biocatalyst, and the lignin dimer were placed in the same compartment (Fig. 3d and Supplementary Fig. 1c). In this environment, lignin conversion can take place in two possible ways: direct lignin conversion by the charge carriers generated by the TiO2 photocatalyst or biocatalytic lignin conversion using LiPH8 with the aid of the photogenerated H2O2. The obtained lignin dimer conversion and selectivity were 37.3% and 34.8%, respectively (Fig. 3e, f). To investigate the role of the enzyme in the single-compartment system, we performed the lignin conversion experiment in the absence of LiPH8. Interestingly, a similar conversion and selectivity were obtained without LiPH8 (Supplementary Fig. 16) and very little H2O2 was generated in the single compartment (Supplementary Fig. 17), which indicates that the reaction mainly proceeds via direct photocatalytic lignin conversion by the TiO2 photocatalyst. The presence of many unidentified peaks using gas chromatography–mass spectroscopy (GC–MS) analysis also revealed that many side reactions take place upon the direct photocatalytic conversion of lignin (Supplementary Figs. 1822). In the single-compartment system, solar light first excites the photocatalyst, generating holes and electrons that initiate the photochemical reaction and generate intermediate radical species (•OH and •O2, respectively). These intermediate radicals can directly attack the biocatalyst, leading to a significant drop in activity. As for other proteins/enzymes, such as chymotrypsin, lysozyme, ribonuclease, and formate dehydrogenase, it was found that LiPH8 in this study also rapidly lost its activity upon irradiation and in the presence of bubbles of O2 gas (Supplementary Fig. 14)45,46,47. In particular, ultraviolet (UV) light directly destroys the protein structures45. Furthermore, gas bubbling also alters the protein structure upon adsorption of the biocatalyst at gas–liquid interfaces46,47. These factors (ROS, light, and O2 gas bubbling) are the main reasons for the low selectivity of the single-compartment system.

In the two-compartment system, the photoanode (H:TiO2) and electrocatalyst cathode (Co–N/CNT) were separated by a Nafion proton exchange membrane, but the cellulose membrane was removed between the cathode and biocatalyst parts (Fig. 3g and Supplementary Fig. 1d). This configuration prevents the direct photochemical lignin conversion observed in the single-compartment system and restrains the deactivation of LiPH8 biocatalyst by the photogenerated holes and •OH radicals in the anodic part. Furthermore, the remaining area was blackened and the H:TiO2 photoanode was covered from behind, as shown in Supplementary Fig. 1e, to shield the biocatalyst from UV light and inhibit its photo-deactivation as in the three-compartment system. The two-compartment cell showed increased selectivity of over 48% (Fig. 3i), which mainly arises from biocatalytic lignin conversion with the help of the in situ photogenerated H2O2 (Supplementary Fig. 23), because only 3% selectivity was obtained when parallel reaction was carried out in the absence of the LiPH8 biocatalyst (Supplementary Fig. 24). However, lignin dimer conversion was still very low (<25%) because the LiPH8 was exposed to O2 bubbles, which are detrimental to enzyme activity (Fig. 3h and Supplementary Fig. 14). Moreover, •O2 radical intermediate generated during the O2 reduction also has an adverse effect on the LiPH8 enzyme activity.

In the three-compartment photo-electro-biochemical system, we verified that the concentrations of •OH and •O2 radicals were very low in the enzyme cell compared to those in the anode and cathode cells, respectively (Supplementary Figs. 25 and 26), resulting in high conversion and selectivity of lignin dimer depolymerisation. The gradual increase of H2O2 concentration in the three-compartment cell is also a reason for the high performance, as this helps to maintain low concentrations of H2O2 in the enzyme cell. When the initial concentrations were 1 and 10 mM, the conversion efficiencies were 82% and 21%, respectively. These values are lower than that of three-compartment system (93.7%) because of enzyme deactivation due to high H2O2 concentration (Supplementary Fig. 27). When we fed a small amount of H2O2 every 15 min, the conversion efficiency was increased, indicating that the continuous and low concentration of H2O2 supply is preferred for the efficient biocatalytic lignin degradation (Supplementary Fig. 28). Turnover frequency (TOF) of the enzyme was 0.036 s−1, which is relatively lower than that of the LiPH8 enzyme reported in the literature48, due to the rate of lignin conversion being limited by H2O2 concentration (Supplementary Fig. 29). These results show that TOF can be controlled in a stable manner by adjusting the H2O2 generation speed of the photo-electro-biochemical system.

Photo-electro-biochemical biopolymer synthesis

The three different types of reactors were also applied for the biopolymer synthesis using coniferyl alcohol, which is one of the three major units of lignin (Supplementary Fig. 30)49. Because current methods of polymer production depend on petrochemicals and, thus, have unavoidable negative environmental effects, polymer synthesis using the abundant, carbon neutral, and recalcitrant lignin biomass is a promising alternative. In the three-compartment photo-electro-biochemical system, biopolymer synthesis reaction was performed with horseradish peroxidase (HRP) biocatalyst with in situ solar H2O2 generation at ambient temperature and pressure (Fig. 4a). The conversion efficiency of coniferyl alcohol monomer and the yield of the biopolymer were 98.3% (Fig. 4b) and 73.3% (Fig. 4c), respectively.

This polymer was comprised of the common linkages between coniferyl alcohol molecules, such as β-O-4, β-β and β-5, and has a number average molecular weight of 1103, which were confirmed by two-dimensional-nuclear magnetic resonance spectroscopy (2D-NMR, Supplementary Fig. 31), and gel permeation chromatography, respectively.

Discussion

In summary, we have demonstrated that a compartmented photo-electro-biochemical system that integrates a photocatalyst, an electrocatalyst, and a biocatalyst, is effective for selective and stable lignin dimer valorisation under solar irradiation without the need for any additional bias or sacrificial agent. In this design, the placement of appropriate membranes as separators between cells protects the biocatalyst from detrimental conditions generated during the reaction, thus preserving its stability and activity. This photo-electro-biochemical system can catalyse lignin dimer cleavage with a 93.7% conversion efficiency and 98.7% selectivity, which far surpasses those of single-compartment (37.3% and 34.8%) and two-compartment (25.0%, 48.1%) systems. The system was further applied for sustainable polymer synthesis using a lignin monomer, coniferyl alcohol, with a 73.3% yield and 98.3% of conversion efficiency; however, the polymer yields of the single-compartment and the two-compartment systems were only ca. 0% and 8.6%, respectively. This unassisted selective lignin valorisation technology could convert waste lignin to value-added aromatics and polymer without the need for any additional energy and chemicals, possibly overcoming the problems associated with current biomass upgradation, such as its low cost effectiveness and limited processing technology. We believe that the development and scaling-up of this technology will be a milestone for the replacement of petrochemicals with biochemicals.

Methods

Preparation of TiO2 photoanode

A rutile TiO2 nanowire film was hydrothermal grown on FTO glass37. First, 15 mL of hydrochloric acid (35%, Samchun Chemical) was diluted with 15 mL deionised (DI) water and mixed with 0.5 mL titanium (IV) butoxide (97%, Aldrich) in a 100 mL beaker. This clear solution and a clean FTO glass substrate were transferred to a Teflon-lined stainless-steel autoclave (125 mL). The sealed autoclave was heated in an oven at 150 °C for 5 h and then cooled to room temperature (RT) slowly. After rinsing with DI water, calcination was performed at 550 °C for 5 h to increase the crystallinity. Finally, the sample was annealed in a hydrogen atmosphere at 350 °C for 30 min38. In addition, an epoxy resin was added behind the TiO2 electrode to block the light transmitted through the TiO2 photoanode. A planar TiO2 film was made on FTO substrate using a radiofrequency sputtering device (SRN-120, SORONA) and calcination was performed at 550 °C for 5 h.

Characterisation of TiO2/FTO

XRD patterns of TiO2 and H:TiO2 films were recorded using a PANalytical X’Pert PRO diffractometer from 10° to 70° in 2θ at a scanning speed of 1° min−1. SEM images were obtained using a Cold FE-SEM (SU8220, Hitach High-Technologies). Optical properties were determined by UV–vis diffuse reflectance spectroscopy using a UV/Vis/NIR spectrophotometer (UV-3600, Shimadzu).

Synthesis of acid-treated carbon nanotubes (AT-CNT)

Before catalyst synthesis, the CNTs were acid-treated to remove metallic impurities. First, 10.0 g of multi-walled CNTs (MR99, Carbon Nanotech Co., LTD) and 715 g of 6 M HNO3 (diluted from 60 wt% HNO3, Samchun Chemical) were mixed and stirred at 80 °C for 12 h. The CNT slurry was filtered, washed with copious amounts of DI water, and dried at 60 °C. The HNO3-treated CNTs were subsequently washed with 700 g of 6 M HCl (diluted from 36 wt% HCl, Samchun Chemical) in the same manner.

Synthesis of the Co–N/CNT catalyst

First, 0.75 g of AT-CNT and 1.50 g of 5,10,15,20-tetrakis(4-methoxyphenyl)-21H,23H-porphine cobalt(II) (CoTMPP, 98%, Porphyrin Systems) were mixed in an agate mortar for 15 min. The mixture was heated at 400 °C under 1 L min−1 N2 flow for 3 h (ramping rate: ca. 2.1 °C min−1). The heat-treated powder and 3.75 mL of tetraethyl orthosilicate (TEOS, 98%, Aldrich) were mixed in the mortar for 5 min. The same volume of formic acid (99.5%, Samchun Chemical) was added to the mixture to initiate TEOS polymerisation. The mixture was dried at 60 °C for 3 h. The dried solid was ground to fine powder and a part (0.60 g) was pyrolyzed at 900 °C under 1 L min−1 N2 flow for 3 h (ramping rate: ca. 2.1 °C min−1). To etch the silica and acid-soluble Co-species, the pyrolyzed powders were added to an acid solution of 4 M HF + 2 M HCl (diluted from 50 wt% HF (JT Baker) and 36 wt% HCl) with a similar volume of ethanol (94.5%, Samchun Chemical) and stirred at RT for 30 min. The suspension was filtered and washed with ethanol and DI water. Acid leaching was repeated once more in the same manner. Finally, the product was dried at 60 °C and collected. Then, the Co–N/CNT-based cathode was prepared by drop-casting catalyst ink on both sides of a carbon paper (0.2 mg cm−2).

Synthesis of the CoTMPP/CNT catalyst

First, 75 mg of AT-CNT was dispersed in 50 mL of N,N-dimethylformamide (DMF, 99.5%, Samchun Chemical) and ultrasonicated for 1 h. During the ultrasonication, CoTMPP in a DMF solution was prepared (10 mg mL−1). The CoTMPP solution (2.3 mL; 23 mg of CoTMPP) was added to the AT-CNT suspension, ultrasonicated for 1 h, and stirred at RT for 12 h. The suspension was centrifuged at 8000 rpm and the supernatant was decanted. The precipitate was washed with DMF twice and anhydrous ethanol and dried at 60 °C. The nominal Co loading was 1 wt%.

Characterisation of Co–N/CNT

XPS measurements were performed with a K-Alpha X-ray photoelectron spectrometer (Thermo Fisher Scientific) with a monochromatic Al Kα X-ray source (1486.6 eV). Co 2p and N 1s XPS spectra were deconvoluted using the XPSPeak41 software with the mixed (Gaussian 70, Lorentzian 30)-function after a Shirley-type background correction. The Co content in Co–N/CNT catalyst was analysed using an inductively coupled plasma-optical emission spectrometer (700-ES, Varian). STEM images were obtained using a JEOL JEM-2100F microscope at an acceleration voltage of 200 kV.

X-ray absorption spectroscopy

X-ray absorption spectroscopy (XAS) was performed at beamline 6D of the Pohang Accelerator Laboratory. The storage ring was operated at an energy of 3 GeV and a beam current of 360 mA. The incident photons were monochromated by Si(111) double crystal, detuned by 30% to remove high-order spectral contamination, and calibrated using a standard Co foil. Co–N/CNT powder sample was pressed using a hand-held pelletiser. Finally, XAS spectra were obtained in transmission detection mode. We also measured the XAS spectrum of CoTMPP. The resulting XAS data were treated using the Athena programme to remove the background and for normalisation52.

Electrochemical characterisation (RRDE)

Electrochemical measurements were conducted using an electrochemical workstation (CHI760E, CH Instruments). The three-electrode system was built for measurement using a graphite rod counter electrode, an Ag/AgCl (saturated KCl filled, RE-1B, ALS) reference electrode, and a catalyst-loaded RRDE (AFE7R9GCPT, Pine Research Instrumentation). Before each use, the RRDE was polished with aqueous 1.0 and 0.3 μm alumina suspensions and a microcloth. The Co–N/CNT catalyst ink was prepared by mixing 10 mg of catalyst, 100 μL of DI water, 13 μL of Nafion dispersion (5 wt%, D521, Dupont), and 1085 μL of anhydrous ethanol. The CoTMPP/CNT catalyst ink was prepared in the same manner but diluted by addition of 300 μL of DI water and 3300 μL of ethanol. The catalyst inks were homogenised using an ultrasonic bath. Then, 6 μL of the catalyst ink was deposited onto the RRDE disk (24 μL for the CoTMPP/CNT catalyst). The resulting catalyst loading was 0.2 mg cm−2. Electrochemical measurements were made both in the 0.1 M phosphate borate solution and 0.1 M HClO4 (diluted from 70% Veritas double distilled, GFS chemicals). After soaking the catalyst-loaded RRDE into a N2-saturated electrolyte, cyclic voltammetry (CV) was performed between 0.05 and 1.20 V (vs. RHE) at a scan rate of 100 mV s−1. Steady CV responses were observed within 20 cycles. The Pt ring of the RRDE was electrochemically cleaned in the same potential range with a scan rate of 500 mV s−1 for 10 cycles. Electrochemical impedance spectroscopy measurement was carried out at 0.68 V (vs. RHE) from 100,000 to 1 Hz at an electrode rotation speed of 1600 rpm in an O2-saturated electrolyte. The series resistance was determined at the high-frequency tail of the Nyquist plot for iR-compensation. The ORR polarisation curve was obtained by LSV from 1.2 to 0.2 V (vs. RHE) at a scan rate of 5 mV s−1 and at different electrode rotation speeds of 2025, 1600, 1225, and 900 rpm for Koutecky–Levich analysis, as shown below.

$$\frac{1}{{i}} = \frac{1}{{{i}_{\mathrm{{{k}}}}}} + \frac{1}{{0.62{nFAD}_{O}^{2/3}{v}^{ - 1/6}{C}_{O}{\omega }^{1/2}}} = \frac{1}{{{i}_{\mathrm{{{k}}}}}} + \frac{1}{{{B} \times {\omega }^{1/2}}}$$
(1)

Here, i, ik, n, F, A, DO, v, CO, and ω represent the measured current, the kinetic current, the electron transfer number, the Faraday constant (96,485 C mol−1), the diffusion coefficient of O2, the kinematic viscosity, the O2 concentration, and the electrode rotation speed, respectively. The plot of i−1 as a function of ω−1/2 gives a line with a slope of B−1, which is used to calculate n. Note that DO, v, and CO values vary with the electrolyte: DO (1.90 × 10−5 and 1.93 × 10−5 cm2 s−1), v (0.010 and 0.0101 cm2 s−1), and CO (1.21 and 1.26 × 10−6 mol cm−3) for 0.1 M phosphate borate solution and 0.1 M HClO4, respectively53,54.

To measure H2O2 yield, the Pt ring potential was held at 1.3 V (vs. RHE) during the LSV measurements, and the H2O2 selectivity was then calculated according to the following equation,

$${{\mathrm{{H}}}}_2{{\mathrm{{O}}}}_2\,{{\mathrm{{selectivity}}}}\,\left( {\mathrm{\% }} \right) = \frac{{200}}{{1 + \frac{{{{N}} \times {i}_{{\mathrm{{d}}}}}}{{{i}_{{\mathrm{{r}}}}}}}}$$
(2)

where id, ir, and N indicate the disk current, the ring current, and the collection efficiency (37%, provided by the manufacturer), respectively. To assess the durability of the catalysts, potential cycling tests were performed between 0.6 and 1.0 V (vs. RHE) with an electrode rotation of 1600 rpm at a scan rate of 50 mV s−1 for 1000 cycles in the O2-saturated electrolyte. After cycling, the ORR activity was measured in a fresh electrolyte.

(Photo-)electrochemical measurements

LSV curves of the H:TiO2 were recorded using a digital multimeter (Ivium-n-Stat Multichannel potentiostat) with the Ag/AgCl reference electrode and a Pt wire counter electrode in 0.1 M phosphate borate solution at pH 4.5 from 0 to 2.00 V (vs. RHE) at a scan rate of 5 mV s−1. The front side of the photoanode (1.33 cm2) was illuminated with the solar simulator (10500, Abet Technologies), and the light intensity was adjusted to 100 mW cm−2 (AM1.5 G) at the sample position using a standard Si cell (PEC-SI01, Peccell Technologies, Inc.). To measure photoanode stability, the chronoamperometric current of H:TiO2 was measured at a constant applied voltage of 1.23 V (vs. RHE) during 12 h. LSV curves of the Co–N/CNT-based cathode (2.0 cm2) were also recorded from 1.2 to 0.05 V (vs. RHE) at a scan rate of 5 mV s−1 in O2-saturated 0.1 M phosphate borate solution at pH 4.5.

Hydrogen peroxide detection

The concentration of H2O2 was estimated using the DPD method55. Depending on the concentration of produced H2O2, the samples were diluted with 0.1 M phosphate borate solution at pH 4.5 or 6.0 in the cases of lignin degradation and biopolymer synthesis, respectively, to avoid exceeding the detection limit of the DPD method. In the case of the powder system, the sample was filtered using a 0.45-μm polytetrafluoroethylene (PTFE) filter (SLCR013NL, Millipore). Furthermore, 0.05 g of N,N-diethyl-1,4-phenylene-diamine sulphate (DPD, ≥ 98.0%, Aldrich) was dissolved in 5 mL of 0.1 N H2SO4 and stored in the dark at 5 °C and 5 mg of peroxidase (POD, horseradish, Sigma) was dissolved in 5 mL DI water and kept at 5 °C. Finally, 2.7 mL of a 0.1 M sodium phosphate buffer (pH 6.0), 0.05 mL of DPD solution, 0.05 mL of POD solution, and 0.2 mL of sample were mixed. The absorbance of mixed solution at λ = 551 nm was measured using a UV/visible spectrophotometer (UV-2600, Shimadzu).

Enzyme stability investigation

To determine the stability of the enzymes against light irradiation and O2 gas purging, LiPH8 and HRP enzymes in 0.1 M phosphate borate solution at pH 4.5 and 6.0 were subject to the same light irradiation and O2 gas purging as the actual lignin conversion experiments. Three sets of experiments (viz., without light irradiation and O2 purging, with light irradiation, and with O2 bubbling) were performed. The residual activity of the enzyme was measured at several points during the 3-h experiment using the oxidation activity of 189 µM 2,2′-azino-bis(3-ethylbenzthiazoline-6-sulfonic acid (ABTS) in the presence of 250 μM H2O2 and 0.1 M Britton–Robinson buffer of pH 3.0. The formation of the product was recorded at 420 nm within 1 min with Ɛ420 nm = 36.7 mM−1 cm−1 using the UV/visible spectrophotometer.

Detection of hydroxyl/superoxide radicals

The formation of •OH was measured using a fluorescence probe method with coumarin56. 0.2 mM coumarin (Aldrich) was added to the 0.1 M phosphate borate solution at the anode and enzyme cell in the three-compartment reactor, and the fluorescence spectra were measured using a fluorescence spectrophotometer (Cray Eclipse, Varian) with the excitation wavelength at 332 nm. Coloration of XTT reduction to XTT–formazam was used for •O2 detection57,58. For this, 0.1 M phosphate borate solution containing 0.1 mM 2,3-bis(2-methoxy-4-nitro-5-sulfophehyl)-2H-tetrazolium-5-carboxanilide (XTT, Aldrich) was added in the cathode and enzyme cell, and the absorbance spectra were recorded from 650 nm to 350 nm using the UV/visible spectrophotometer.

Enzyme preparation

The LiPH8 synthetic gene, including the seven-residue pro-sequence, was synthesised by Bioneer Company (South Korea). The gene coding protein sequence was retrieved from UniProtKB database (P06181). LiPH8 was expressed as inclusion body in Escherichia coli BL21 (DE3) and reactivated through in vitro refolding procedure as previously reported59 with slight modification. The inclusion body was added into the refolding solution containing 100 mM Tris–HCl pH 8.0, CaCl2 2 mM, guanidine hydrochloride 0.36 M, l-glutathione oxidised form 0.7 mM and stirred overnight at 4 °C. The refolded solution was concentrated and buffer-exchanged with sodium acetate buffer 100 mM at pH 4.0 then pH 6.0 before subjected for purification. The anion-exchange chromatography with Mono Q 5/50 GL column (GE Healthcare Life Sciences Co., USA) was used for purification step in this study. The column was equilibrated with sodium acetate 10 mM, pH 6.0 (buffer A) and eluted with a linear gradient of buffer B—sodium acetate 500 mM, pH 6.0. The highest activity fraction of LiPH8 was tested with sodium dodecyl sulfate–polyacrylamide gel electrophoresis and used for this study. HRP type VI was purchased from Aldrich Co. (USA) and used without any further purification.

Photo-electro-biochemical lignin conversion

The overall reaction was performed in an acryl reactor composed of an anode cell with a quartz window on one side, a cathode cell, and an enzyme cell. In the case of the three-compartment reactor, the anode cell was separated from cathode cell through a Nafion membrane (Nafion® 117, 0.18 mm thick, Aldrich), and the cathode cell was separated from an enzyme cell through a cellulose membrane (Spectra/Por®, 6–8 kDa, Spectrum). For the lignin dimer conversion, 0.1 M phosphate borate solution of pH 4.5 was used as the electrolyte. The anode cell, cathode cell, and enzyme cell consisted of H:TiO2 photoanode (1.33 cm2) with 8 mL electrolyte, Co–N/CNT-based cathode (2.0 cm2) with 4 mL electrolyte, and 0.5 mM of lignin dimer and 0.8 μM of LiPH8 in 8 mL electrolyte, respectively. The photoanode and cathode were connected to each other with alligator clips and copper wire as an external circuit. In the case of the two-compartment reactor without an enzyme cell, the cathode cell was composed of the Co–N/CNT cathode, 0.5 mM of lignin dimer, and 0.8 μM of the LiPH8 in 4 mL electrolyte. In the single cell, Degussa P25 TiO2 powder (0.5 mg mL−1) used as a photocatalyst for H2O2 production, 0.5 mM of lignin dimer, and 0.8 μM of the LiPH8 enzyme were added together in 8 mL electrolyte. The photoanode (or P25 photocatalyst) was illuminated using a solar simulator (10500, Abet Technologies) at 100 mW cm−2 (AM1.5 G). O2 gas was continuously bubbled into the cathode electrolyte from 20 min before the reaction until the reaction was completed. The biopolymer synthesis was performed in the three kinds of the reactors as depolymerisation of lignin with slight modifications. The reactions were carried out with 0.5 mM of coniferyl alcohol as a substrate and 1.4 μM of the HRP as an enzyme in 0.1 M phosphate borate solution at pH 6.0.

Identification of phenolic compounds

The completed reaction mixture was analysed by high-performance liquid chromatography (HPLC). The HPLC procedure was performed by injecting fractions using an Agilent 1200 HPLC system onto a reverse-phase Eclipse XDB-C18 column (4.6 × 150 mm, 5 μm, Agilent). Gradient separation was performed using 0.1% aqueous trifluoroacetic acid (solvent A) to methanol/acetonitrile (25:75; v/v; solvent B) with the following conditions: analysis time of 15 min flow of 1.5 mL min−1 and column temperature of 30 °C. The gradient programme was as follows: 0 min—15% B, 6 min—60% B, 11.5 min—100% B, and 13 min—0% B. Before injection, the sample was filtered through a hydrophilic 0.2-μm PTFE membrane filter. The products were identified relative to an authentic library of standards based on their retention times and UV absorption spectra. The quantification of the reaction was performed by HPLC based on a linear external standard curve (R2 > 0.95) of the respective compound. For the by-products, the phenolic derivatives were extracted with dichloromethane and analysed using a GC–MS (Agilent) with a DB-5MS (60 m × 250 μm × 0.25 μm) column. The oven temperature was elevated from 50 to 280 °C. The product mass spectrum was identified using an authentic library of standards.

Characterisation of the polymer

The polymer was collected by centrifugation at 13,000 rpm within 10 min, washed three times with 2 N HCl solution, and dried under vacuum conditions. The polymer yield was determined by UV analysis at 280 nm based on a linear external standard curve (R2 > 0.95) of the respective synthesised dehydrogenative polymer from coniferyl alcohol. The dried polymer was dissolved in tetrahydrofuran (THF) at a concentration of 3 mg mL−1. The solution was filtered using a 0.2 μm PTFE filter and analysed by gel permeation chromatography, for which THF was used as eluent with a flow rate of 1 mL min−1. Samples were detected at 280 nm and polystyrene standard used for calibration curves. For 2D 13C–1H heteronuclear single quantum correlation (HSQC) analysis, the polymer was dissolved in 0.5 mL DMSO-d6 before NMR analysis. NMR spectra from the polymer were acquired on a 400 MHz FT-NMR (Bruker) instrument with a 5 mm BBO NMR probe. The central DMSO solvent peak was used as an internal reference (δH/δC 2.50/39.52 ppm). The HSQC parameters and NMR chemical assignments followed previously published methods60.

Data availability

All data are available from the corresponding author upon request.

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Acknowledgements

This research was supported by the National Research Foundation (NRF) funded by the Ministry of Science and ICT (nos. NRF-2017M1A2A2087630, NRF-2017R1D1A1B03035450, and NRF-2017R1A2B2008464) and the 2018 Research Fund (1.180006.01) of Ulsan National Institute of Science and Technology (UNIST). The X-ray absorption spectroscopy experiments performed at beamlines 6D and 10C of the Pohang Accelerator Laboratory (PAL) were supported in part by the Ministry of Science and ICT, POSTECH, and UNIST.

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Contributions

J.-W.J., Y.H.K., and S.H.J. proposed, designed, and directed the research. J.-W.J., M.K., L.T.M.P., and Y.J.S. conceived the concept of the compartmented photo-electro-biocatalyst system. M.K. and L.T.M.P. prepared the photocatalysts with D.O. and the biocatalysts with T.V.T.N., respectively, and measured the conversion efficiency and selectivity for lignin valorisation. Y.J.S. prepared and characterised the electrocatalysts and measured their performances with the help of J.W. and J.H.K. P.S., J.R., and T.J.S. helped to analyse the data and provided valuable input. M.K., L.T.M.P., Y.J.S., S.H.J., Y.H.K., and J.-W.J. co-wrote the manuscript. All authors read and commented on the manuscript.

Corresponding authors

Correspondence to Sang Hoon Joo or Yong Hwan Kim or Ji-Wook Jang.

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Peer review information Nature Communications thanks Jonathan Bloh, and the other, anonymous, reviewer(s) for their contribution to the peer review of this work. Peer reviewer reports are available.

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Ko, M., Pham, L.T.M., Sa, Y.J. et al. Unassisted solar lignin valorisation using a compartmented photo-electro-biochemical cell. Nat Commun 10, 5123 (2019). https://doi.org/10.1038/s41467-019-13022-7

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