We developed an efficient and environmentally friendly two-step tandem methodology for the synthesis of sugar-containing coumarin derivatives catalyzed by lipozyme TL IM from
Thermomyces lanuginosus in continuous-flow microreactors. Compared to those observed for other methods, the salient features of this work including green reaction conditions, short residence time (50 min), and catalysts are more readily available and the biocatalysis reaction process is efficient and easy to control. This two-step tandem synthesis of coumarin derivatives using the continuous-flow technology is a proof of concept that opens the use of enzymatic microreactors in coumarin derivative biotransformations.An effective and environmentally friendly two-step tandem protocol for the synthesis of sugar-containing coumarin derivatives catalyzed by lipozyme TL IM in continuous-flow microreactors has been developed.
Coumarins and their derivatives have attracted considerable attention due to their extensive biological activities such as anti-bacterial, antiviral, anticancer, and antioxidant properties.
1 Numerous studies including the separation and purification of naturally occurring coumarins from a variety of plants as well as the chemical synthesis of coumarin compounds with novel structures and properties have been conducted for the research and development of coumarins as potential drugs.
2 So far, some coumarins, for example, warfarin,
3 an anticoagulant that acts as a vitamin K antagonist, have been widely used in the treatment of thrombosis. Armillarisin A and novobiocin are commonly used as antibiotics ().
4Open in a separate windowDrugs containing coumarin structures.As important coumarin derivatives, sugar-containing coumarin compounds have attracted special interest in organic synthesis and medicinal research due to their excellent physicochemical and pharmacokinetic characteristics.
5 Thorson
et al.6 reported that the glycosylation of the classical pharmacophore warfarin fundamentally alters the drug''s mechanism of action, leading to a dramatic reduction in the anticoagulant function and a concomitant marked increase in anticancer cytotoxicity. In the past few years, several works on the synthesis of sugar-containing coumarins have been reported. Supuran
et al.7 synthesized a series of glycosyl coumarin carbonic anhydrase IX and XII inhibitors, which strongly attenuated the growth of primary breast tumors. In 2016, Nilsson
et al.8 reported a selective galactose-coumarin-derived galectin-3 inhibitor, which displayed efficacy similar to that of a known nonselective galectin-1/galectin-3 inhibitor.The construction of sugar-containing coumarin derivatives can be achieved by basic synthetic approaches, and the most common synthesis strategy is the chemical method,
9 which always needs several “protection–deprotection” steps. Recently, visible light has been used in the glycosylation reaction; however, most of the protocols for photoinduced glycosylation require transition metal catalysts in combination with expensive additives for the reaction to proceed.
10Enzymes are the most efficient catalysts, offering much more competitive processes compared to chemical catalysts.
11 The use of enzymes as catalysts for the preparation of novel compounds has received increasing attention over the past few years. Some enzymes, such as the engineered C-glycosyltransferase MiCGTb-GAGM, were applied for the synthesis of coumarin C-glycosides, and two of them exhibited potent SGLT2 inhibitory activities.
12 Nidetzky synthesized a new sugar-containing coumarin catalyzed by O-glycosyltransferase.
13 Some other enzymes such as BLAP (alkaline protease from
Bacillus licheniformis) have also been used to synthesize coumarin.
14 The reactions catalyzed by enzymes are relatively mild; however, they always require a longer reaction time (24 h or more) to achieve the desired yields, and the enzymes needed for the reaction are difficult to obtain.
15Continuous-flow microreactors coupled with enzymes have become an efficient way to increase the reaction efficiency and improve the yield.
16 Modern synthetic chemistry faces the challenge of providing the society with high-performing, valuable products that are environmentally benign, cost-effective, safe, and atom-efficient. Due to a high surface-to-volume ratio, better heat exchange, and efficient mixing, the continuous-flow microreactor technology (MRT) has become increasingly popular as an alternative to conventional batch chemistry synthesis.
17 In particular, with respect to the 12 principles of green chemistry, MRT can play a major role in improving chemical processes.
18 To explore novel, eco-friendly and highly efficient protocols for sugar-containing coumarins and also as part of our ongoing study on the tandem microreaction technology, herein, we have reported a two-step tandem synthesis process of sugar-containing coumarin derivatives catalysed by lipozyme TL IM from
Thermomyces lanuginosus in continuous-flow microreactors. The aim of this paper is to investigate using a two-step tandem continuous-flow microreactor the effect of various reaction parameters on the reaction yield. Furthermore, we hope to quickly build the related compound library through a new synthesis method for future drug screening ().
Open in a separate windowSynthesis of sugar-containing coumarin derivatives in continuous-flow microreactors.First, in order to determine whether lipozyme TL IM can be used to catalyze coumarin intermediates or sugar-containing coumarin synthesis reactions, we chose salicylaldehyde (1a) and diethyl malonate (2a) to react at 50 °C for 24 h in a shaker reactor (. It was found that the rate of the reaction catalyzed by the mixed catalyst was faster than that of the reaction catalyzed by K
2CO
3, especially in the range of 0–8 h. After 16 h, the product 3a catalyzed by the mixed catalyst reached equilibrium. Although the yield of 3a after catalysis by 25 mg K
2CO
3 peaked after 24 hours, it was not as high as the yield obtained after catalysis by the mixed catalyst.Effect of reaction solvents and catalysts on the synthesis of coumarin under shaker reactors
a |
---|
Entry | Solvent | Catalysts | Yieldb (%) |
---|
1 | DMSO | None | n.d. |
2 | DMSO | 100 mg lipozyme TL IM (denatured) | n.d. |
3 | Acetone | 100 mg lipozyme TL IM | 23 |
4 | DMSO | 100 mg lipozyme TL IM | 25 |
5 | tert-Amyl alcohols | 100 mg K2CO3 | <5 |
6 | Ethanol | 100 mg K2CO3 | 35 |
7 | Acetone | 100 mg K2CO3 | 61 |
8 | DMSO | 100 mg K2CO3 | 72 |
9 | DMSO | 50 mg K2CO3 | 78 |
10 | DMSO | 25 mg K2CO3 | 80 |
11 | DMSO | 5 mg K2CO3 | 71 |
12 | DMSO | 25 mg K2CO3/80 mg lipozyme TL IM | 84 |
13 | DMSO | 25 mg K2CO3/120 mg lipozyme TL IM | 85 |
14 | DMSO | 25 mg K2CO3/160 mg lipozyme TL IM | 83 |
Open in a separate windowaReaction conditions: salicylaldehyde (1a) (50 mM), diethyl malonate (2a) (100 mM), catalysts in 5 mL solvent, at 50 °C for 24 h.
bIsolated yields.
Open in a separate windowThe influence of reaction time on the synthesis of coumarin under shaker reactors. General reaction conditions: salicylaldehyde (1a) (50 mM), diethyl malonate (2a) (100 mM), catalysts in 5 mL DMSO at 50 °C.For the synthesis of sugar-containing coumarins, considering that the enzyme and reaction media play a vital role in the reaction, we studied the effects of solvents and enzymes on the reaction (
Open in a separate windowaReaction conditions: ethyl coumarin-3-carboxylate (3a) (50 mM),
d-glucose (4a) (25 mM), catalysts (200 mg) in 5 mL solvent, at 50 °C for 24 h.
bIsolated yields.
d-Glucose (4a) contains multiple hydroxyl groups, including 6-OH, 1-OH and secondary OHs. The acylation position of
d-glucose was verified by
13C NMR according to the general strategy described by Yoshimoto
et al.19 The
13C NMR data are shown in
|
---|
Carbon atom | d-Glucose | 5a | 5e | 5i | 5m | 5q |
---|
C-6α | 61.20 | 65.22 | 65.32 | 65.19 | 65.26 | 64.82 |
C-6β | 61.20 | 65.22 | 65.36 | 65.19 | 65.26 | 64.82 |
C-5α | 71.80 | 69.20 | 69.18 | 69.22 | 69.21 | 69.24 |
C-5β | 76.70 | 73.49 | 73.48 | 73.51 | 73.50 | 73.55 |
C-4α | 70.58 | 70.57 | 70.50 | 70.58 | 70.59 | 70.61 |
C-4β | 70.30 | 70.17 | 70.10 | 70.18 | 70.19 | 70.22 |
C-3α | 73.04 | 72.91 | 72.90 | 72.95 | 72.91 | 72.91 |
C-3β | 76.79 | 76.46 | 76.45 | 76.49 | 76.46 | 76.47 |
C-2α | 72.29 | 72.16 | 72.14 | 72.21 | 72.18 | 72.17 |
C-2β | 74.78 | 74.71 | 74.68 | 74.75 | 74.72 | 74.71 |
C-1α | 92.12 | 92.38 | 92.39 | 92.44 | 92.41 | 92.36 |
C-1β | 96.79 | 97.00 | 97.01 | 97.06 | 97.02 | 96.98 |
Open in a separate windowEncouraged by these results, we wanted to design a two-step tandem continuous-flow protocol for the synthesis of sugar-containing coumarin derivatives. The experimental setup consisted of two flow microreactor systems: two syringe pumps (Harvard apparatus PHD 2000), two microtube reactors (R1 and R2) and two Y-shaped mixers (Y1 and Y2,
φ = 1.8 mm) (). The microtube reactor R1 was filled with K
2CO
3/lipozyme TL IM (catalyst reactivity: 250 IUN g
−1) and the microtube reactor R2 was filled with lipozyme TL IM. The whole flow microreactor system was dipped in a water bath to control the reaction temperature. A solution of the salicylaldehyde derivative (8.0 M) in DMSO and diester malonate derivative (16.0 M) in DMSO was passed through R1 (internal diameter 2.0 mm, length 100 cm) by a syringe pump with a flow rate of 62.4 μL min
−1. The outlet mixture was mixed with a solution of sugar (50 mM in DMSO/
tert-amyl alcohol) in Y2 and passed through R2 (flow rate: 15.6 μL min
−1). After the reaction, the discharge was collected in a glass vessel. A final yield of 43–75% was obtained by column chromatography after the solvent was removed by vacuum distillation. The pure product was characterized by
1H NMR,
13C NMR and ESI-MS.
Open in a separate windowThe experimental setup of two-step tandem sugar-containing coumarin derivative synthesis in microreactors.We studied the reaction parameters of each step before the two-step tandem synthesis of sugar-containing coumarin derivatives in continuous-flow microreactors. For the coumarin intermediate synthesis reaction, we selected the reaction of salicylaldehyde (1a) and diethyl malonate (2a) as the model reaction and studied the effect of the substrate molar ratio, catalysts, reaction temperature and residence time on the reaction. The results are summarized in
Open in a separate windowaReaction conditions: feed 1, salicylaldehyde (1a) was dissolved in 10 mL DMSO; feed 2, diethyl malonate (2a) was dissolved in 10 mL DMSO, reacted in continuous-flow microreactors catalyzed by mixed catalyst K
2CO
3/lipozyme TL IM.
bMass ratio of K
2CO
3 to mixed catalyst K
2CO
3/lipozyme TL IM.
cIsolated yields.After we obtained the optimal synthesis conditions for the coumarin intermediates in the first step, we continued to study the optimal reaction conditions for the sugar-containing coumarins in the second step, including reaction solvents, substrate ratio, reaction temperature and residence time. We chose the reaction of ethyl coumarin-3-carboxylate (3a) and
d-glucose (4a) as the template reaction.
tert-Amyl alcohol was selected as the reaction solvent according to our results obtained for the batch method (entry 3, ). Excess DMSO can cause enzyme inactivation; thus, we chose DMSO :
tert-amyl alcohol = 1 : 18 as the optimal reaction solvent for the enzymatic synthesis of sugar-containing coumarin derivatives in continuous-flow microreactors.
Open in a separate windowThe effect of volume ratio of DMSO to
tert-amyl alcohol on the sugar-containing coumarin synthesis reaction in continuous-flow microreactors.We then studied the effects of the molar ratio of ethyl coumarin-3-carboxylate (3a) to
d-glucose (4a) on the synthesis reaction of sugar-containing coumarins in continuous-flow microreactors. We studied the substrate ratio of ethyl coumarin-3-carboxylate (3a) to
d-glucose (4a) from 1 : 3 to 5 : 1; we found that with the increase in ethyl coumarin-3-carboxylate (3a), the yield of the reaction increased correspondingly (). When the molecular ratio of ethyl coumarin-3-carboxylate (3a) to
d-glucose (4a) reached 4 : 1, the best reaction yield of 51% was obtained. Therefore, the molar ratio of ethyl coumarin-3-carboxylate (3a) :
d-glucose (4a) = 4 : 1 was chosen as the optimal substrate ratio for the next step of reaction exploration.
Open in a separate windowThe effect of the molar ratio of ethyl coumarin-3-carboxylate to sugar on the sugar-containing coumarin synthesis reaction in microreactors.For enzymatic reactions, the reaction temperature is a very important reaction parameter; thus, we continued to study the effect of reaction temperature on the reaction yield. We studied the reaction temperature from 30 °C to 60 °C and found that the reaction could occur at 30 °C and reached the optimal level at 35 °C. After this, the reaction temperature continued to increase, but the yield rate of the reaction did not improve (). Therefore, the optimal reaction temperature for the synthesis of sugar-containing coumarins in the second step is 35 °C.
Open in a separate windowThe effect of reaction temperature on the sugar-containing coumarin synthesis in microreactors.In continuous-flow microreactors, the residence time/flow rate has a great influence on the reaction yield. Therefore, we studied the effect of the residence time/flow rate on the reaction yield of sugar-containing coumarins in microreactors. We investigated the reaction from 10 min to 60 min and found that when the residence time was 10 min and the reaction flow rate was 62.4 μL min
−1, 38% yield could be obtained. As the residence time was extended, the reaction yield also gradually increased. The best yield,
i.e., 65% of sugar-containing coumarins was observed for a residence time of 40 min at a flow rate of 15.6 μL min
−1. Thereafter, the residence time was extended, and the yield of the reaction did not increase correspondingly (). Therefore, the residence time/flow rate of 40 min/15.6 μL min
−1 was chosen as the optimal residence time/flow rate for the enzymatic synthesis of sugar-containing coumarins in microreactors.
Open in a separate windowThe effect of residence time on the sugar-containing coumarin synthesis reaction in microreactors.After obtaining the optimal reaction conditions for the two-step reaction, it was considered that the R
4 group in compound 3 had a great influence on the synthesis of sugar-containing coumarin derivatives. Therefore, we chose compounds 3a, 3b and 3c to react with
d-glucose (4a) (
Open in a separate windowaReaction conditions: feed 1, coumarin-3-carboxylate derivative (2.0 mmol) was dissolved in
tert-amyl alcohol/DMSO; feed 2,
d-glucose (4a) (0.5 mmol) was dissolved in
tert-amyl alcohol/DMSO, reacted in continuous-flow microreactors catalyzed by lipozyme TL IM (870 mg) at 35 °C for 40 min.
bIsolated yields.Finally, we explored the scope and limitations of this two-step tandem methodology for the synthesis of sugar-containing coumarin derivatives catalyzed by lipozyme TL IM from
Thermomyces lanuginosus in continuous-flow microreactors (
Open in a separate windowaFeed 1, salicylaldehyde derivative (20 mmol) was dissolved in 2.5 mL DMSO; feed 2, dimethyl malonate (2b) (40 mmol) was dissolved in 2.5 mL DMSO, reacted in continuous-flow microreactors catalyzed by mixed catalyst K
2CO
3/lipozyme TL IM (104.4 mg K
2CO
3 and 765.6 mg lipozyme TL IM) at 40 °C for 10 min; feed 3, 0.52 mL above reaction solution mixed with 9.48 mL
tert-amyl alcohol; feed 4, sugar (0.5 mmol) was dissolved in 0.52 mL DMSO and 9.48 mL
tert-amyl alcohol, reacted in continuous-flow microreactors catalyzed by lipozyme TL IM (870 mg) at 35 °C for 40 min.
bIsolated yields.In conclusion, we have developed an effective and environmentally friendly two-step tandem methodology for the synthesis of sugar-containing coumarin derivatives catalyzed by lipozyme TL IM from
Thermomyces lanuginosus in continuous-flow microreactors. Lipozyme TL IM was first used to catalyze coumarin intermediates and sugar-containing coumarin synthesis reactions. For the first time, we designed two-step continuous flow reactors and used them in the synthesis of sugar-containing coumarins. We studied the effects of various reaction parameters including the reaction medium, substrate molar ratio, reaction temperature, residence time/flow rate and the effect of the substrate structure on the reaction. Using this technique, 18 sugar-containing coumarin derivatives were rapidly synthesized. Compared to traditional methods, the salient features of this method include mild reaction conditions (40 °C for the first step and 35 °C for the second step), short residence time (10 min for the first step and 40 min for the second step), high yields, and the use of an enzyme as a catalyst, resulting in high regioselectivity without the need for protection-deprotection steps. Furthermore, the two-step tandem continuous-flow synthesis protocol avoids the separation of intermediates and simplifies the experimental steps, which make our methodology a valuable contribution to the field of the synthesis of sugar-containing coumarin derivatives. The obtained sugar-containing coumarin derivatives may be potentially bioactive and can be used as pharmacological alternatives. We will continue our research to quickly build a library of related compounds for subsequent drug screening.
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