Perspectives for biocatalytic lignin utilization: cleaving 4-O-5 and Cα–Cβ bonds in dimeric lignin model compounds catalyzed by a promiscuous activity of tyrosinase
© The Author(s) 2017
Received: 29 May 2017
Accepted: 5 September 2017
Published: 11 September 2017
In the biorefinery utilizing lignocellulosic biomasses, lignin decomposition to value-added phenolic derivatives is a key issue, and recently biocatalytic delignification is emerging owing to its superior selectivity, low energy consumption, and unparalleled sustainability. However, besides heme-containing peroxidases and laccases, information about lignolytic biocatalysts is still limited till date.
Herein, we report a promiscuous activity of tyrosinase which is closely associated with delignification requiring high redox potentials (>1.4 V vs. normal hydrogen electrode [NHE]). The promiscuous activity of tyrosinase not only oxidizes veratryl alcohol, a commonly used nonphenolic substrate for assaying ligninolytic activity, to veratraldehyde but also cleaves the 4-O-5 and Cα–Cβ bonds in 4-phenoxyphenol and guaiacyl glycerol-β-guaiacyl ether (GGE) that are dimeric lignin model compounds. Cyclic voltammograms additionally verified that the promiscuous activity oxidizes lignin-related high redox potential substrates.
These results might be applicable for extending the versatility of tyrosinase toward biocatalytic delignification as well as suggesting a new perspective for sustainable lignin utilization. Furthermore, the results provide insight for exploring the previously unknown promiscuous activities of biocatalysts much more diverse than ever thought before, thereby innovatively expanding the applicable area of biocatalysis.
KeywordsSustainable lignin utilization Tyrosinase Promiscuous activity 4-Phenoxyphenol Guaiacyl glycerol-β-guaiacyl ether (GGE)
Biocatalysis is a useful and environmentally friendly approach in the fields of organic chemistry, pharmaceuticals, and biorefinery [1, 2]. To widen the enzymatic functionality of hoped-for reactions, some researchers have aimed to discover an overlooked inherent catalytic potential offered by nature known as catalytic promiscuity [3, 4]. Catalytic promiscuity is the ability of an enzyme to catalyze alternate reactions distinctly different from its primary catalysis  and a key factor in the evolution of new enzymatic functions from few ancestral generalist enzymes [3, 6]. Thus, the catalytic promiscuity of enzymes has been shown to be capable of catalyzing the hoped-for reactions through novel biocatalytic routes, thereby expanding the versatility of those enzymes .
Depletion of fossil fuels and climate change have accelerated research interest and effort on developing biorefinery using microbial fermentation which utilizes sugars obtained from lignocellulosic biomasses. Fermentable sugars are usually obtained from cellulosic and hemicellulosic components in biomasses by saccharification, whereas lignin is just pretreated for efficient saccharification. Thus, the strategy for utilizing lignin as sustainable feedstock for producing value-added phenolic derivatives is not still enough yet . Even though various chemical pretreatments have been attempted in biorefinery, recently ligninolytic biocatalysts for pretreatment are emerging due to their superior selectivity, lower energy consumption, and unparalleled sustainability [9, 10]. In nature, heme-containing peroxidases such as lignin peroxidase (LiP, E.C. 126.96.36.199), manganese peroxidase (MnP, E.C. 188.8.131.52), versatile peroxidase (VP, E.C. 184.108.40.206), and dye-decolorizing peroxidase (DyP, E.C. 220.127.116.11) are known to be involved in delignification by catalyzing two-electron oxidation requiring a high redox potential of over +1.4 V (vs. normal hydrogen electrode [NHE]) with hydrogen peroxide as an electron acceptor [11, 12]. However, hydrogen peroxide, inevitably required for the catalysis of heme-containing peroxidases, often leads to critical inactivation by attacking and destroying the heme in the active site . Laccase (E.C. 18.104.22.168) catalyzing low- or mid-redox potential compounds (usually < 1.0 V vs. NHE) is sometimes categorized as a ligninolytic biocatalyst; natural (e.g., vanillin) and artificial mediators (e.g., 2,2′-azinobis-(3-ethylbenzthiazoline-6-sulfonate) [ABTS] and 1-hydroxybenzotriazole [HBT]) often enhance the laccase activity for delignification . Besides heme-containing peroxidases and laccase, information on other ligninolytic biocatalysts is very limited to date.
In order to broaden the enzymatic diversity of pretreating lignocellulosic biomasses and to increase the information about ligninolytic biocatalysts, we focused on tyrosinase (E.C. 22.214.171.124) which shows two catalytic activities for various phenolic compounds using O2 as the electron acceptor: o-hydroxylation of monophenol to diphenol by a cresolase activity and oxidation of diphenol to quinone by a catecholase activity . In addition, we paid special attention to the fact that lignin is a highly branched phenolic-based natural polymer and thus evaluated whether tyrosinase possesses a promiscuous activity associated with delignification. In this study, it was verified that (i) tyrosinase has a promiscuous activity for oxidizing veratryl alcohol which is the most commonly used nonphenolic substrate for assaying ligninolytic activity; (ii) cyclic voltammogram additionally shows the promiscuous activity for oxidizing lignin-related high redox potential substrate; and (iii) the promiscuous activity cleaves the 4-O-5 and Cα–Cβ bonds in phenolic lignin model dimers independently of cation mediators (e.g., ABTS).
Results and discussion
Tyrosinase has a promiscuous activity for oxidizing a lignin-related nonphenolic substrate
Kinetic parameters of tyrosinase and lignin peroxidase (LiP) using veratryl alcohol as the substrate
k cat (s−1)
K m (mM)
k cat/K m (s−1mM−1)
Activity (U mg−1)
Lignin peroxidase (LiP)
Cyclic voltammetry verifies that tyrosinase has a catalytic promiscuity for oxidizing a nonphenolic lignin-related substrate with a high redox potential
The promiscuous activity of tyrosinase cleaves the 4-O-5 and Cα–Cβ bond in dimeric lignin model compounds
Because the substrate, GGE, was not detected under the GC–MS conditions used for the vanillin analysis (using a HP-Innowax column), derivatization with tetramethylsilane (TMS) was carried out to analyze GGE. As a result, GGE-TMS was detected at a retention time of 26.1 in a GC–MS equipped with a HP-Ultra2 column (Additional file 1: Fig. S1, Table S1). In the HPLC profile (Fig. 4a), one unidentified peak at 18.929 min was also observed in the reaction sample. GC–MS analysis indicated that the estimated m/z value of the unidentified product was of 272 (Additional file 1: Table S1). It is not clear how the unidentified product was formed. A possible mechanism would be a further conversion of catalytic product (other than vanillin) to an unidentified product by tyrosinase. In accordance with Ahmad et al., bacterial DyP, one of the ligninolytic heme-containing peroxidases, catalyzes GGE to vanillin and guaiacol . In addition, Chen et al. validated that DyP from Thermomonospora curvata would have a potential for lignin degradation and proposed the catalytic mechanism for decomposing GGE to guaiacol oligomer . Besides DyP, ligninolytic heme-containing peroxidases have been known to easily convert guaiacol to guaiacol-oligomer [12, 19, 24]. As with DyP from Rhodococcus jostii RHA1 , the catalytic promiscuity of tyrosinase seemed to cleave the Cα–Cβ bond in GGE, yielding vanillin (Fig. 4c) and possibly an unstable o-(2-hydroxyethyl)guaiacol radical. The unstable o-(2-hydroxyethyl)guaiacol radical might be further catalyzed to guaiacol and 2-hydroxyacetaldehyde by the tyrosinase, and then guaiacol might be polymerized to an unidentified product with a m/z of 272 as shown in Fig. 4c: given that (i) the reduction of compound II to resting state in DyP initiates the conversion of o-(2-hydroxyethyl)guaiacol to guaiacol  and (ii) the redox potential of compound II/resting state in peroxidases is estimated ranging from +0.93 to +1.26 V , the promiscuous activity of tyrosinase oxidizing a high redox potential substrate veratryl alcohol (+1.22 V) might convert o-(2-hydroxyethyl)guaiacol to guaiacol. Additionally, Garcia-Molina et al. demonstrated the catalytic activity of tyrosinase on guaiacol . Therefore, the promiscuous activity of tyrosinase seemed to directly cleave the Cα–Cβ bond according to vanillin formation and possibly guide the cleavage of the β-O-4 bond in GGE. However, further identification on the degradation products of GGE by tyrosinase is required to elucidate the degradation mechanism.
Given that tyrosinase exhibits a broad substrate specificity for various phenolic compounds and that lignin is a highly branched phenolic-based natural polymer, we herein explored the novel promiscuous activity of tyrosinase closely associated with delignification. Tyrosinase not only oxidizes veratryl alcohol, the most widely used nonphenolic substrate for assaying ligninolytic activity, but also cleaves the 4-O-5 and Cα–Cβ bonds in dimeric lignin model compounds. Consequently, tyrosinase seems to be applicable for biocatalytic pretreatment in biorefinery utilizing lignocellulosic biomass as a sustainable feedstock. Furthermore, the results provide a new perspective for sustainable lignin utilization to produce value-added phenolic derivatives.
Even if higher substrate specificity is a unique feature of a biocatalyst distinguishable from a chemical catalyst, recently reported promiscuous activities have been considered as favorable properties in numerous applications . In accordance with Nam et al., the higher substrate specificity in a biocatalyst is a result of the evolution from promiscuous activities in ancestral generalist biocatalysts . In this study, we, for the first time, identified the valuable catalytic promiscuity of tyrosinase associated with delignification. The results discussed herein could extend the versatility of tyrosinase as a promising ligninolytic biocatalyst under mild operational conditions (neutral pH using O2 as the electron acceptor). Given that the higher substrate specificity in a biocatalyst is a result of the evolution from promiscuous activities , the results provide insight into further understanding of how the lignocellulose-degrading biocatalytic specificity has evolved from promiscuous ancestral biocatalysts which might be much more diverse than ever thought before.
Tyrosinase has been studied for a long time in various fields including in bioremediation for detoxifying phenolics , in pharmaceutics for L-DOPA production [15, 33, 34], and in bioelectronics for detecting phenolics . Nevertheless, the structure-based catalytic mechanism of tyrosinase has not been actively discussed until Matoba et al. reported the X-ray crystal structure of tyrosinase from Streptomyces castaneoglobisporus . Based on the recently verified structure of tyrosinase from Agaricus bisporus (PDB ID:2Y9W) [37, 38], we will aim to suggest a catalytic mechanism for the promiscuous activity in the near future.
Enzymes and chemicals
Tyrosinase from Agaricus bisporus, LiP from Phanerochaete chrysosporium, veratryl alcohol (96%), veratraldehyde (99%), 4-phenoxy phenol (99%), benzyl phenyl ether (98%), dimethyl sulfoxide (DMSO, 99%), and benzyl benzoate (99%) were purchased from Sigma-Aldrich (St. Louis, USA). GGE (97%) and trimethylchlorosilane (TMCS, 1%) in N,O-bis(trimethylsilyl) trifluoroacetamide (BSTFA) [BSTFA + TMCS] were purchased from Tokyo Chemical Industry Co., Ltd (Tokyo, Japan) and Supelco analytical (Bellefonte, USA), respectively. To remove trace impurities such as metal salts, tyrosinase was solubilized in phosphate buffer (50 mM, pH 6.5) and then purified with an ultrafiltration device with a cutoff of 10 kDa (Merck Millipore, MA, USA). All other chemicals were used as the highest grade available without further purification.
The catalytic promiscuity of tyrosinase was tested with the following substrates: 10 mM veratryl alcohol. Due to the low solubility in the aqueous phase, 0.5 mM of 4-phenoxyphenol and GGE were used in phosphate buffer (pH 6.5) and 0.625% DMSO, respectively. The reaction was initiated by adding 100 (for veratryl alcohol and 4-phenoxyphenol) or 500 U (for GGE) of tyrosinase into 1 mL of a substrate solution in 50 mM phosphate buffer (pH 6.5). One U of tyrosinase converts 1 μmol of l-tyrosine to L-DOPA per min at pH 6.5 and 25 °C. All reactions were conducted at 30 °C for 24 h.
After a 24-h reaction, the catalytic products from veratryl alcohol, 4-phenoxyphenol, and GGE were identified by GC–MS. The analytes were extracted with ethyl acetate (for veratryl alcohol, veratraldehyde, 4-phenoxyphenol, and phenol) or methyl chloride (for GGE and vanillin), and then, GC–MS analysis was performed with a 6890N GC interfaced with a 5975 MS (Agilent Technologies, Santa Clara, USA) under the following conditions: a fused polyethylene glycol HP-INNOWax capillary (30 m × 0.25 mm i.d., 0.25 μm, Agilent Technologies, Santa Clara, USA) and He (99.9999%) were used as the column and carrier gas at a constant flow rate (1.2 mL min−1), respectively. To analyze GGE, TMS derivatization was performed with BSTFA + TMCS, and a HP-Ultra2 column was used. Mass spectrometry was conducted in the electron impact mode (70 eV), and the ion source temperature was 230 °C. The temperature program of the oven is summarized in Additional file 1: Table S2. Chromatographic peaks were identified by the retention time and the mass spectra library (NIST02). Authentic standard chemicals were used to confirm the identification.
A one-compartment electrochemical cell was constructed with a 3-electrode system for cyclic voltammetry. Glassy carbon, coiled Pt wire, and Ag/AgCl were used as the working, counter, and reference electrodes, respectively. Cyclic voltammetry was carried out using a potentiostat/galvanostat (WMPG1000K8, WonA Tech., Seoul, Korea) controlled by commercial WMPG software. In all cyclic voltammetries, the scan rate and the scan range were 50 mV s−1 and −1.5 to +1.5 V, respectively.
To determine the kinetic parameters, various concentrations of veratryl alcohol (0.1, 0.25, 0.5, 1.0, 2.0, and 5.0 mM) were used, and the initial increase of absorbance was monitored at 310 nm (εveratraldehyde,310 nm = 9.3 mM−1 cm−1) with a UV-spectrophotometer (Shimazhu, UV-1240, Kyoto, Japan) at 30 °C . To calculate the kinetic parameters shown in Table 1, the kinetic data were fitted into the Michaelis–Menten equation.
GGE and vanillin were analyzed by HPLC (Agilent 1200 HPLC system, CO, USA). The HPLC procedure was performed by injecting fractions using a reverse-phase Eclipse XDB-C18 column (4.6 × 150 mm, 5 μm, Agilent). Gradient separation was performed from distilled water (solvent A) to methanol (solvent B) using the following conditions: flow rate 1.0 mL min−1, column temperature 25 °C, time 0 min-5% B, time 5 min-25% B, time 10 min-40% B, time 30 min-50% B, time 35 min-100% B. Using a UV detector at 280 nm, authentic GGE and vanillin were detected at 13.522 and 10.497 min, respectively.
KM and YU conceived the study. KM performed experimental works and wrote the manuscript. TY and JK carried out MS analysis under supervision of YK. YHK reviewed and commented on the manuscript. HMW, BS, and YJY participated in coordination of the manuscript draft. All authors read and approved the final manuscript.
The authors would like to thank Dr. Sunghee Ahn at the Korea Research Institute of Standards and Science (KRISS) for the kind discussion about the GC–MS analysis of GGE and vanillin.
The authors declare that they have no competing interests.
Availability of data and materials
All data generated or analyzed during the study are included in this manuscript and Additional file.
Consent for publication
All authors approved the manuscript.
This work was supported by the National Research Foundation of Korea (NRF) funded by the Ministry of Education, Science, and Technology (NRF-2009-C1AAA001-0093286), and Korea Evaluation Institution of Industrial Technology funded by Ministry of Trade, Industry, and Energy (10049675). This work was also supported by the National Research Council of Science and Technology (NST) granted by the Korean government (MSIP) (No. CAP-11-04-KIST).
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