Open Access Article
André
Taborda
,
Márcia
Rénio
,
M. Rita
Ventura
* and
Lígia O.
Martins
*
Instituto de Tecnologia Química e Biológica António Xavier, Universidade Nova de Lisboa, Av da República, 2780-157 Oeiras, Portugal. E-mail: lmartins@itqb.unl.pt
First published on 17th December 2024
Rare sugars are monosaccharides and disaccharides highly valued for their unique properties and beneficial health effects. Their scarcity has led to inefficient extraction from natural sources, prompting the development of several chemical and enzymatic methods to improve their synthesis. In this study, we aim to optimize a regio- and stereoselective chemo-enzymatic process for synthesizing the rare sugar D-allose. We use a bacterial glycoside-3-oxidase that oxidizes D-Glc at the C2 or C3 position, depending on the presence of a C1 substitution, being converted into the respective keto-derivatives. Through protein engineering, we improve the enzyme's catalytic activity for D-Glc by 20-fold after seven rounds of directed evolution and increase its operational stability by 10-fold. The engineered enzyme uses 1-O-benzyl-D-glucoside as substrate, ensuring regioselective oxidation at the C3 position, followed by a stereoselective chemical reduction and deprotection step, affording D-allose with an overall yield of 81%. This innovative strategy represents a novel, straightforward approach for synthesizing D-allose, avoiding laborious, time-consuming purifications and complicated and lengthy protection–deprotection strategies. Importantly, it shows potential for synthesizing other rare C3 epimers of biomass sugars through eco-friendly and cost-effective processes, with applications in pharmaceuticals and food technology.
Various chemical and enzymatic methods have been developed to address their production. These include (i) chemical isomerization, which is typically unselective, resulting in complex product mixtures,6 (ii) selective oxidation of minimally protected sugars followed by reduction,7–10 and (iii) site-selective radical epimerization reactions that produce rare sugars from biomass-derived carbohydrates.11 Enzymatic methods provide regio- and stereo-specificity under milder conditions, making them attractive, sustainable alternatives to traditional chemical synthesis.12 Over the past two decades, most studies on the enzymatic synthesis of rare sugars have utilized a strategy known as Izumoring. This approach enables the cyclical conversion of monosaccharides through enzymatic epimerization, isomerization and oxidation-reduction.13,14 Nevertheless, other non-Izumoring enzymatic techniques have also emerged.12,15 For example, pyranose-2-oxidases (P2Oxs) from the glucose-methanol-choline (GMC) family, can synthesize D-tagatose and D-glucopyranosyl-β-1,6-D-mannopyranose from D-galactose and gentiobiosone by promoting the oxidation of hexoses at the C2 position, respectively, using P2Ox oxidation followed by a chemical reduction.16,17
This work focuses on the chemo-enzymatic synthesis of the rare sugar D-allose, a C3 epimer of D-glucose (D-Glc), as studies exploring the enzymatic synthesis of C3 compared to C2 epimeric rare sugars are more scarce. D-Allose has gained significant attention for its beneficial properties as a non-caloric sweetener,18 anticancer,19–21 anti-oxidant,22 anti-inflammatory,23 anti-hypertensive24 and immunosuppressor agent.25 Despite its various benefits, D-allose remains a minor player in the industrial market due to its limited availability and high production costs.26 Earlier approaches included synthesizing β-D-allose from D-ribose mediated by cyanohydrin27 and later by reducing 1,2:5,6-di-O-isopropylidene-α-D-ribo-hexofuranose-3-ulose hydrate in 68–70% overall yield.28 More recently, the oxidation steps were mediated by other chemicals;7,8,10,29 however, these processes often lead to inconsistent and sometimes very low yields, as well as the formation of undesirable by-products, thus, the need for tedious purification steps, and occasionally the use of highly specialized equipment.
Multi-enzymatic reactions involving isomerases and epimerases starting from D-Glc via a three-pathway enzyme reaction having as intermediates D-fructose and D-psicose have become a common D-allose synthesizing strategy;30 nevertheless, due to the reversibility of these enzymes’ reactions, the resulting final reaction mixtures are complex complicating the target product purification and resulting in low final yields. Recently, an one-pot reaction reportedly produced D-allose from D-fructose using D-allulose 3-epimerase and D-ribose-5-phosphate isomerase with a conversion yield of 13%.31
We have recently characterized a bacterial glycoside-3-oxidase (PsG3Ox)32 that shares high sequence similarities with fungal P2Oxs.33,34 G3Ox oxidizes C-glycosides at the C3 position of the sugar moiety at high catalytic efficiency while exhibiting residual activity for monosaccharides, such as D-Glc.32,35–37 Herein, we engineered G3Ox to improve its catalytic properties towards D-Glc using directed evolution, an approach used successfully in recent years in our group to enhance the properties of various enzymes.38–42 We show that the optimized enzyme can selectively oxidize the C3–OH group of partially protected D-Glc at improved rates and with complete regioselectivity.
Given the enzyme's broad substrate specificity and potential for further engineering, this system is a promising pathway for synthesizing rare sugars, creating economic opportunities for their industrial production and commercialization.
:
vector 1
:
10 using the NEBuilder HiFi DNA Assembly Master Mix (New England Biolabs). The ligation was performed at 50 °C for 1 h, and afterward, it was used to transform E. cloni 10 G elite cells, allowing the propagation of the library. The plasmid library was extracted to transform electrocompetent KRX cells in a Gene Pulser Xcell™ (Bio-Rad Laboratories) under defined conditions (C = 10 μF, PC = 600 Ω, V = 1.8 kV). The cell suspension was spread on solid media containing 100 μg ml−1 of ampicillin and 0.1% rhamnose.
000 M−1 cm−1) was measured using a Synergy2 microplate reader (BioTek).
300 M−1 cm−1) was measured to assess the functional fraction of enzyme preparations (e.g., for kinetic measurements).
The enzymatic oxidation of benzyl-glucoside was performed using 20 mg of 1-O-Benzyl-α/β-D-glucopyranoside, 5 U ml−1 of the 16F10 variant and 0.1 mg ml−1 of catalase (Sigma-Aldrich) in a total volume of 1.5 ml in water (adjusted to pH 7.5–8.0). The reaction proceeded for 24 hours at 25 °C under magnetic stirring to facilitate oxygenation of the solution. The reaction progress was monitored by TLC in Merck 60 F254 silica gel plates (90/10 ethyl acetate/methanol). At the end of the reaction time, the enzymes were removed by ultrafiltration using a 30 kDa Amicon (Merck) at 4000 rpm in an Eppendorf centrifuge. The reaction product was lyophilized and purified by flash column (Kieselgel 60, 0.032–0.063 mm) with 100% ethyl acetate to afford 1-O-benzyl-3-keto-α/β-D-glucopyranoside (2α and 2β; 1.4
:
1 α/β) in 36% yield as a viscous colourless syrup. 1H NMR (400 MHz, MeOH-d4): δ 7.46–7.27 (m, 10H, Ar–H), 5.28 (d, J = 4.40 Hz, 1H, H1-α), 5.00 (d, J = 11.97 Hz, 1H, CH2–Bn), 4.76 (dd, J = 12.09 Hz, J = 3.00 Hz, 2H, CH2–Bn), 4.61 (d, J = 11.92 Hz, 1H, CH2–Bn), 4.48 (d, J = 7.94 Hz, 1H, H1-β), 4.45 (dd, J = 4.38 Hz, J = 1.24 Hz, 1H, H2-α), 4.29–4.25 (m, 2H, H4-α and H4-β), 4.22 (dd, J = 7.90 Hz, J = 1.65 Hz, 1H, H2-β), 3.99 (dd, J = 12.20 Hz, J = 2.03 Hz, 1H, H6-β), 3.88–3.79 (m, 3H, H6-β and H6-α), 3.75 (ddd, J = 9.70 Hz, J = 4.50 Hz, J = 2.30 Hz, 1H, H5-α), 3.38–3.34 (m, 1H, H5-β). 13C NMR (100 MHz, MeOH-d4): δ 205.7 (C3-α), 205.6 (C3-β), 137.2 (Ar–C-β), 137.0 (Ar–C-α), 128.0, 127.9, 127.8, 127.7, 127.5, 127.4 (Ar–C), 103.3 (C1-β), 100.6 (C1-α), 77.0 (C5-β), 76.9 (C2-β), 75.7 (C5-α), 74.7 (C2-α), 72.3 (C4-α), 72.0 (C4-β), 70.6 (CH2–Bn-β), 69.2 (CH2–Bn-α), 61.2 (C6-β), 60.0 (C6-α) ppm. HRMS: m/z: [M + H2O]+ calcd for C13H20O7 286.1053; found 286.1287.
For the conversions with the β anomer, the oxidation reaction was performed using 20 mg of 1-O-benzyl-β-glucopyranoside, 1 U ml−1 of the 16F10 variant, 0.1 mg ml−1 of catalase in a total volume of 1.5 mL in water (adjusted to pH 7.5–8.0). The reaction proceeded for 6 h 30 m at 25 °C with magnetic stirring. The reaction was monitored as above, and the enzyme was removed by ultrafiltration. The 1-O-benzyl-3-keto-β-D-glucopyranoside 2β was lyophilized overnight and obtained in quantitative yield (100%) as a viscous colourless syrup. [α]20D = −75.61 (c 1.2, MeOH). 1H NMR (400 MHz, MeOH-d4): δ 7.45–7.43 (m, 2H, Ar–H), 7.37–7.28 (m, 3H, Ar–H), 5.0 (d, J = 11.93 Hz, 1H, CH2–Bn), 4.75 (d, J = 11.77 Hz, 1H, CH2–Bn), 4.48 (d, J = 7.89 Hz, 1H, H1), 4.27 (dd, J = 10.19 Hz, J = 1.66 Hz, 1H, H4), 4.22 (dd, J = 7.88 Hz, J = 1.73 Hz, 1H, H2), 3.99 (dd, J = 12.01 Hz, J = 2.05 Hz, 1H, H6), 3.85 (dd, J = 12.05 Hz, J = 4.89 Hz, 1H, H6), 3.36 (dd, J = 4.96 Hz, J = 2.08 Hz, 1H, H5) ppm. 13C NMR (100 MHz, MeOH-d4): δ 205.8 (C-3), 137.3 (Ar–C), 128.0, 127.8, 127.5 (Ar–C), 103.3 (C1), 76.9 (C2), 76.8 (C5), 72.3 (C4), 70.7 (CH2–Bn), 61.2 (C6) ppm. HRMS: m/z: [M + H2O]+ calcd for C13H20O7 286.1053; found 286.1050.
:
THF (2
:
1, 2 mL) and the reaction was stirred for 2 h at 0 °C. The excess LS-selectride was removed by adding acidic ion exchange resin (Dowex DVB WX8 H+-form), and the mixture was filtered and concentrated under vacuum. The crude product was purified by flash column (Kieselgel 60, 0.032–0.063 mm) with 90
:
10 ethyl acetate/methanol to afford the 1-O-benzyl-β-D-allopyranoside 3 (36 mg) in 86% of yield as a viscous colourless syrup. [α]20D = −66.36 (c 1.2, MeOH). 1H NMR (400 MHz, MeOH-d4): δ 7.45–7.43 (m, 2H, Ar–H), 7.36–7.26 (m, 3H, Ar–H), 4.95 (d, J = 11.74 Hz, 1H, CH2–Bn), 4.76 (d, J = 7.78 Hz, 1H, H1), 4.67 (d, J = 11.74 Hz, 1H, CH2–Bn), 4.07 (t, J = 2.92 Hz, 1H, H3), 3.92–3.87 (m, 1H, H6) 3.74–3.68 (m, 2H, H5 and H6), 3.53 (dd, J = 9.37 Hz, J = 3.01 Hz, 1H, H4), 3.40 (dd, J = 7.99 Hz, J = 3.01 Hz, 1H, H2) ppm. 13C NMR (100 MHz, MeOH-d4): δ 137.9 (Ar–C), 127.9, 127.8, 127.2 (Ar–C), 99.6 (C1), 74.1 (C5), 71.6 (C3), 71.0 (C2), 70.3 (CH2–Bn), 67.6 (C4), 61.8 (C6) ppm. HRMS: m/z: [M + Na]+ calcd for C13H18NaO6 293.0996; found 293.0996.
The compound 3 (24 mg, 0.089 mmol) in MeOH (2 mL) was hydrogenated at 50 psi in the presence of Pd/C 10% (0.08 g) overnight. Then, the reaction mixture was filtered through Celite and washed with MeOH; the solvent evaporated to afford D-allose 4 (15 mg) in 94% yield as a viscous colourless syrup, major anomer β. 1H NMR (400 MHz, MeOH-d4): δ 5.06 (d, J = 3.45 Hz, 1H, H1-α), 4.85 (d, J = 7.89 Hz, 1H, H1-β), 4.06 (t, J = 3.00 Hz, 1H, H3-β), 3.85 (dd, J = 11.62 Hz, J = 2.26 Hz, 1H, H6-β), 3.78–3.71 (m, 1H, H5-β), 3.68–3.63 (m, 1H, H6-β), 3.54–3.48 (m, H4-β), 3.26 (dd, J = 7.99 Hz, J = 2.99 Hz, 1H, H2) ppm. 13C NMR (100 MHz, MeOH-d4): δ 94.0 (C1-β), 93.8 (C1-α), 74.1 (C5-β), 72.2 (C2-β), 71.6 (C3-β), 67.6 (C4-β), 61.9 (C6-β) ppm. HRMS: m/z: [M + Na]+ calcd for C6H12NaO6 203.0526; found 203.0528.
000 variants were screened, and one hit variant (16F10) was identified with improved activity for D-Glc (Fig. 1 and Table 1).
![]() | ||
| Fig. 1 Lineage of variants of PsG3Ox generated during the enzyme engineering. The variants’ names are highlighted in a colored box, and the mutations in the variants’ genotypes are listed below. In the initial round, the variant screened with the highest activity, variant 1A1, emerged with a single mutation (G366S). In the second round, the best variant, 5D5, showcases three additional mutations (A75T, A206T, Q295H). In the third round, the selected best variant, 41G6, harbored an additional single mutation (P336S). The fourth round yielded two variants, 2G4 and 7E9, with comparable activities, and their genes underwent epPCR followed by DNA shuffling to retain mutually beneficial mutations. At this point, stability screening was introduced simultaneously with activity screening, leading to the selection of variant 2B9, which exhibited four-fold increased stability at 40 °C compared to variant 7E9. DNA shuffling between 2B9 and the wild-type was performed, eliminating putative deleterious mutations while preserving enzyme properties. The resulting variant, 6E3, bearing only six mutations, displayed similar activity and stability to 2B9 with ten mutations. In a final round of epPCR using 6E3 as a template, variant 16F10, due to the replacement of I357 V and D383N, exhibited a 1.5-fold activity improvement. All screening details are summarized in Table S3.† | ||
| Optimal pH | k cat (s−1) | K m (M) | k cat/Km (M−1 s−1) | |
|---|---|---|---|---|
| Activity was measured using the HRP-AAP/DCHBS coupled assay. All reactions were performed in 100 mM sodium phosphate buffer at the optimal pH and 37 °C. The kinetic parameters were determined by fitting the data directly on the Michaelis–Menten equation using OriginLab. | ||||
| Wild-type | 7.5 | 0.2 ± 0.05 | 0.37 ± 0.13 | 0.5 ± 0.1 |
| 1A1 | 7.5 | 0.4 ± 0.1 | 0.54 ± 0.11 | 0.7 ± 0.1 |
| 5D5 | 8.5 | 1.0 ± 0.2 | 0.33 ± 0.05 | 3.2 ± 0.4 |
| 41G6 | 8.0 | 1.2 ± 0.2 | 0.24 ± 0.05 | 5.1 ± 0.2 |
| 2G4 | 8.0 | 1.9 ± 0.2 | 0.26 ± 0.05 | 6.7 ± 0.8 |
| 7E9 | 8.0 | 2.3 ± 0.3 | 0.27 ± 0.05 | 8.6 ± 0.4 |
| 2B9 | 8.0 | 2.6 ± 0.3 | 0.23 ± 0.06 | 10.6 ± 0.9 |
| 6E3 | 8.0 | 3.0 ± 0.2 | 0.26 ± 0.01 | 11.5 ± 0.6 |
| 16F10 | 8.0 | 4.8 ± 1.0 | 0.37 ± 0.05 | 11.4 ± 0.8 |
All enzyme variants were purified (Table S4†), and the percentage of the functional enzyme (i.e., with a full complement of FAD) ranged from 20 to 60%. The optimal pH (7.5) of wild-type for D-Glc was up-shifted by 0.5 to 1 unit in the second round (variant 5D5). The catalytic performance of the evolutionary intermediates and the hit variant was assessed. We show that throughout the engineering process, the turnover number (kcat) significantly improved, representing the most notable difference in catalytic parameters, positively impacting the catalytic efficiency (kcat/Km) observed for D-Glc among the variants in the later generations (Table 1). In contrast, the Km, a parameter associated with substrate affinity, remained unchanged during the evolutionary pathway. Previous studies have emphasized that these enzymes’ active site topology and oligomeric state are key factors affecting substrate specificity within P2Oxs (tetramer)/G3Oxs (monomer) sub-families despite their high sequence similarity.32,37 Indeed, despite the observed improvements in variants of PsG3Ox, the kcat for D-Glc of the hit variant 16F10 remains 10- to 20-fold lower than those observed for D-Glc in fungal P2Oxs such as TmP2Ox and PcP2Ox, whereas the Km value is three orders of magnitude higher (Table S5†).
The activity of variant 16F10 was also tested against a diverse array of substrates, including different mono-, di- and trisaccharides, as well as one aminosugar, glucosamine (Table 2) and remarkably, it exhibited increased activity for most of the tested substrates. The highest enhancements were measured for D-maltose and D-galactose, with activity increasing ∼35-fold compared to the wild-type. D-Glc and lactose followed, demonstrating around a 20-fold increase than the wild-type.
| Specific activity (nmol min−1 mg−1) | ||
|---|---|---|
| Wild-type | 16F10 | |
| Activity was measured using the HRP-AAP/DCHBS coupled assay. All reactions were performed with 100 mM substrate in 100 mM sodium phosphate buffer at pH 7.5 and 25 °C. Nd – not detected. | ||
| Monosaccharides | ||
| D(+)-Glucose | 36.9 ± 5.7 | 645.4 ± 164.4 |
| D(+)-Galactose | 2.9 ± 0.7 | 97.1 ± 21.6 |
| L(+)-Arabinose | 5.3 ± 0.9 | 68.2 ± 4.8 |
| 2-Deoxy-glucose | 3.2 ± 0.5 | 44.2 ± 7.7 |
| D(−)-Ribose | 2.6 ± 1.8 | 24.3 ± 4.0 |
| L(+)-Rhamnose | 1.4 ± 0.1 | 8.9 ± 1.7 |
| D(+)-Mannose | 0.3 ± 0.2 | 3.2 ± 0.1 |
| D(−)-Fructose | 0.3 ± 0.1 | 1.6 ± 0.5 |
| L(−)-Fucose | 0.5 ± 0.1 | 3.6 ± 1.0 |
| Disaccharides | ||
| D-Lactose | 0.6 ± 0.4 | 10.8 ± 2.8 |
| D(+)-Maltose | 0.2 ± 0.1 | 7.3 ± 1.5 |
| D(+)-Trehalose | 0.2 ± 0.03 | 1.8 ± 1.0 |
| Trisaccharides | ||
| D(+)-Raffinose | 0.2 ± 0.1 | Nd |
| Aminosugars | ||
| D(+)-Glucosamine | 1.3 ± 0.3 | 0.5 ± 0.3 |
| Variant | T Appm (°C) | T agg (°C) | t 40 °C1/2 (min) |
|---|---|---|---|
| Apparent melting temperatures (TAppm) were measured by steady-state fluorescence following the intrinsic fluorescence of the enzyme, aggregation temperature (Tagg) was monitored by static light scattering and half-life time at 40 °C (t40 °C1/2) was measured by following the loss activity over time. The activity at each time point was measured using the HRP-AAP/DCHBS system. | |||
| Wild-type | 49 ± 2 | 50 | 27 ± 2 |
| 1A1 | 47 ± 3 | 46 | 366 ± 46 |
| 5D5 | 47 ± 3 | 49 | 374 ± 82 |
| 41G6 | 44 ± 1 | 43 | 5 ± 1 |
| 2G4 | 43 ± 1 | 43 | 82 ± 8 |
| 7E9 | 44 ± 2 | 45 | 102 ± 18 |
| 2B9 | 47 ± 2 | 46 | 291 ± 30 |
| 6E3 | 45 ± 2 | 48 | 212 ± 41 |
| 16F10 | 44 ± 2 | 48 | 187 ± 30 |
Regarding the kinetic, so-called, long-term or operational stability, which quantifies the amount of enzyme that loses activity irreversibly during incubation at a specific temperature, the first two variants (1A1 and 5D5) exhibited a remarkable 10-fold improvement in the stability as compared to wild-type (27 min at 40 °C). In contrast, variant 41G6, in the 3rd round, showed a substantial trade-off between activity and stability, with a slight increase in kcat (Table 1) but at a high cost of kinetic stability: ∼100-fold decrease in half-life time (5 min at 40 °C) (Table 3 and Fig. S2†). The kinetic stability quantifies the amount of enzyme that denaturates irreversibly owing to protein aggregation, misfolding, and covalent changes.48 The wild-type and different variants deactivate according to a first-order process, which the classical Lumry can describe–Eyring model applied to the majority of enzymes (N ↔ U → D, where N, U and D are the native, the reversible unfolded and the irreversible denatured enzyme), pointing to a simple pathway of unfolding and denaturation. Since this effect was due to a single mutation, P336S, we have introduced and removed this mutation in different genetic backgrounds. The replacement of P336S in the wild-type has not affected activity but led to a pronounced decrease in the half-life time at 40 °C, making impossible its measurement (Tables S6 and S7†); in contrast, its removal from subsequent variants 2G4, 7E9, and 2B9 (4th and 5th round) result in a significant increase in stability but at expenses of a 2-fold decreased activity (Tables S6 and S7†). These observations suggest that P336S has influenced the evolutionary trajectory of the enzyme towards improved activity for D-Glc and indicate that it exhibits genotype-dependent effects hinting at epistatic interactions.49 The mutations introduced in subsequent rounds of evolution compensated the negative effect of P336S, and all subsequent variants show increased stability, retaining 50% of activity after 80 to 290 min at 40 °C (Table 3). It is important to mention that during the first four generations, the screening of variant libraries during the directed evolution was based solely on activity measurements, which led to the selection of variant 41G6 with unexpectedly low kinetic stability after purification. From the fourth generation onward, we simultaneously screened for activity and stability, selecting only those variants that performed well in both properties. Notably, as mentioned, the hit variant 16F10 exhibited a kcat approximately 20-fold higher, and a half-life time at 40 °C, almost 10-fold higher than the wild-type enzyme (Tables 1 and 3; Fig S1†).
![]() | ||
| Fig. 2 Visual representation and molecular details of the mutations introduced in the hit variant 16F10. (A) Cartoon representation of wild-type PsG3Ox structure (PDB 7QF8) with all mutations present in 16F10 represented by the Cα as spheres and colored according to the round in which they were introduced (Fig. 1). The insertion-1 region and substrate loop are colored in dark blue and orange, respectively. All mutations are located distal to FADN5 (B) detailed view, close to FAD, with D-Glc docked and the two mutations (G366S, Q295H) closer to the active site. The FAD is colored yellow, the D-Glc is colored orange, the catalytic residues (H440 and N484) are colored light blue, and the non-catalytic interacting residues with D-Glc (R94, T129, Q297, Q340) are colored grey. | ||
:
1) and tested the enzymatic activity of wild-type and engineered variant 16F10, which shows higher selectivity for C3 over C2 (Table 4; Fig. S4†). Comparing the catalytic parameters obtained, 16F10 showed a 10-fold increase in the turnover number (kcat). At the same time, the Km remained unchanged as compared to the wild-type enzyme. Interestingly, regarding the Km values, a 25-fold decrease was observed for the substrate 1-O-benzyl-α/β-D-glucopyranoside compared to D-Glc (Table 4). These results are consistent with our previous findings, which highlight the crucial role of an aromatic aglycone in facilitating substrate access and binding to the active site.32
| Variant | k cat (s−1) | K m (mM) | k cat/Km (M−1 s−1) | |
|---|---|---|---|---|
| Activity for D-Glc, 1-O-benzyl-α/β-D-glucopyranoside and 1-O-Benzyl-β-D-glucopyranoside was measured using the HRP-AAP/DCHBS coupled assay. All reactions were performed in 100 mM sodium phosphate buffer at the optimal pH and 37 °C. The kinetic parameters were determined by fitting the data directly on the Michaelis–Menten equation using OriginLab. | ||||
| D-Glc | Wild-type | 0.2 ± 0.05 | 370 ± 130 | 0.5 ± 0.1 |
| 16F10 | 4.8 ± 1.0 | 370 ± 50 | 11.4 ± 0.8 | |
| 1-O-Benzyl-α/β-D-glucopyranoside | Wild-type | 0.06 ± 0.01 | 13.4 ± 3.8 | 5.0 ± 1.0 |
| 16F10 | 0.57 ± 0.05 | 17.4 ± 1.3 | 33.0 ± 1.0 | |
| 1-O-Benzyl-β-D-glucopyranoside | Wild-type | 0.31 ± 0.01 | 16.4 ± 4.0 | 19.3 ± 5.2 |
| 16F10 | 1.26 ± 0.07 | 11.3 ± 1.0 | 111.5 ± 4.0 | |
The oxidation product of 1-O-benzyl-α/β-D-glucopyranoside was characterized by NMR, confirming the presence of the ketone at C3 (Fig. S5 and S6†). However, a partial conversion (36% yield) was obtained, even after 24 h reaction. Interestingly, the β-anomer was the predominant isomer present in the NMR spectra, which indicated some stereoselectivity for this isomer. Therefore, the β-isomer (1-O-benzyl-β-D-glucopyranoside) was synthesized,43 and the enzyme's activity was tested towards this substrate. The obtained catalytic parameters confirmed that the β-anomer is more efficiently oxidized than the α-anomer, as observed by the increase of the kcat parameter and also reflected in catalytic efficiency (kcat/Km) (Table 4). A bioconversion reaction using the 1-O-benzyl-β-D-glucopyranoside 1 as substrate (20 mg of the substrate in a volume of 1.5 ml) was performed, and a total conversion (100% yield) was obtained, affording 1-O-benzyl-3-keto-β-D-glucopyranoside 2 (Scheme 1) with complete regioselectivity and without the need of further purification (Fig. S7 and S8†).
The current chemical strategies for the regioselective oxidation of unprotected or semi-protected monosaccharides at the C3 position primarily rely on a Pd/neocuproine catalyst and benzoquinone, yielding good results (Table S9†).7,10 Despite its effectiveness, these methods require a palladium catalyst and a chemical terminal oxidant, which have a significant environmental impact. Also, in the case of some substrates, a mixture of C3/C4 oxidation products was obtained, requiring additional purification steps. A metal-free strategy was also developed using electrochemical oxidation of the C3 position, mediated by quinuclidine.29 However, the obtained yields are lower, specific equipment is required, and, in some cases, it is necessary to protect the C6 position of the pyranosides (Table S9†).
In contrast, the enzymatic oxidation of 1-O-benzyl-β-glucopyranoside at the C3 position is complete and efficient, avoiding hazardous chemicals and preventing the formation of by-products, thereby eliminating the need for extensive purification.
The following step involved the stereoselective reduction of the resulting compound 2 to afford 1-O-benzyl-β-D-allopyranoside 3 (Scheme 1; Fig. S9 and S10†). The allose-derived product has an inverted configuration at the C3 position compared to D-Glc, with the 3-OH group positioned cis to the vicinal 2-OH and 4-OH groups. Different reducing agents were studied to obtain the best yield and cis selectivity (Table 5).
| Reagent | Solvent | Yield (%) | Diastereomeric ratio 1 : 3 |
|---|---|---|---|
| All reactions were performed at 0 °C. The ratio of diastereomers 1 and 3 obtained after reduction with LS-Seletride was determined by 1H NMR. | |||
| NaBH4 | MeOH | 63 | 1 : 1.5 |
| K-Selectride® | DMSO : THF (2 : 1) |
64 | 0 : 1 |
| LS-Selectride® | DMSO : THF (2 : 1) |
86 | 0 : 1 |
Reduction with NaBH4 afforded a mixture of the two diastereomeric alcohols 1 and 3 with very low selectivity towards the cis (alloside 3) product. K- and LS-Selectride provided exclusively the corresponding C3 cis-alcohol 3 (Scheme 1); however, LS-selectride afforded the highest yield (86%, Table 5). The high 1,2-cis stereoselectivity of selectride is well documented. It is attributed to the steric bulk of the reducing agent-inducing attack at the side opposite to a vicinal group in cyclohexanones, which usually forms the axial alcohol predominantly.10,52,53 To finally obtain D-allose, the removal of the anomeric benzyl protecting group was easily accomplished by hydrogenation, affording exclusively D-allose 4 (Scheme 1; Fig. S11 and S12†) in 94% yield, without the need for purification. In conclusion, a new efficient regio- and stereoselective chemo-enzymatic method was developed to synthesize the rare sugar D-allose in 81% overall yield.
Despite some progress, synthesizing D-allose using chemical and enzymatic approaches still presents several challenges (Table S9†). While chemical methods can achieve viable yields, they are often associated with high production costs due to expensive catalysts and environmental hazards from chemical waste.26 The biosynthetic production of D-allose, mainly through the Izumoring strategy, is a more environmentally friendly and scalable alternative that has emerged as the leading industrial method despite the low production allose yields.26 The new chemo-enzymatic approach described here offers several advantages over existing methods: the first enzymatic step is selectively efficient, and no by-products were formed. The two successive chemical reactions are also very selective and effective using common reagents, requiring only a single, straightforward chromatographic purification step after the carbonyl reduction with LS-selectride. Since no by-products were formed, complex purification is unnecessary, contrasting with reported methods. Considering the affordability of the starting material, the completeness and irreversibility of the enzymatic oxidation, and the high yields obtained in the stereoselective reduction, our process has strong potential for scaling up to industrial production of D-allose.
Footnote |
| † Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d4gc04449e |
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