Daniel Paprockia,
Dominik Koszelewskia,
Anna Żądłoa,
Peter Waldeb and
Ryszard Ostaszewski*a
aInstitute of Organic Chemistry, Polish Academy of Sciences, Kasprzaka 44/52, 01-224 Warsaw, Poland. E-mail: ryszard.ostaszewski@icho.edu.pl
bLaboratory of Polymer Chemistry, Department of Materials, ETH Zurich, Vladimir-Prelog-Weg 5, 8093 Zurich, Switzerland
First published on 13th July 2016
A new, green route for the synthesis of α-acyloxy carboxamides from an alcohol, a carboxylic acid and an isocyanide was developed. The reaction comprises the aerobic oxidation of an alcohol to the corresponding aldehyde, catalyzed by the Trametes versicolor laccase/TEMPO system, followed by a one pot Passerini reaction in an aqueous surfactant medium. The influence of different types of surfactants on the reaction efficiency was investigated. The best results were obtained by employing dioctadecyldimethylammonium bromide (DODAB), a known vesicle-forming cationic surfactant. Importantly, apart from the metalloenzyme used, the described procedure toward α-acyloxy carboxamides is metal-free and does not require hazardous organic solvents, what makes it environmentally friendly.
Various methods for the preparation of α-acyloxy carboxamides have been reported in the literature. Standard protocols usually require equimolar amounts of a coupling agent like N,N′-dicyclohexylcarbodiimide (DCC) and a catalyst like 4-(dimethylamino)pyridine (DMAP),10 which is corrosive and very toxic.11 Furthermore, these reactions require organic solvents like dichloromethane. Moreover, overall yields of multistep syntheses are moderate.
A convenient way of obtaining α-acyloxy carboxamides is to use a three component reaction between a carboxylic acid, a carbonyl compound and an isocyanide, first described by Passerini in 1921.12 This Passerini-three component reaction (P-3CR) is usually performed in aprotic organic solvents, e.g. dichloromethane or toluene, which are toxic and carcinogenic.13 To eliminate this inconvenience, the Passerini reaction can also be conducted under solvent free conditions.14 However, in this case at least one substrate has to be in liquid state. Pirrung, Das Sarma and others have shown that for certain substrates the P-3CR can be performed efficiently also in water.15 Furthermore, we have recently demonstrated that the application of aqueous suspensions of DODAB (dioctadecyldimethylammonium bromide), a vesicle-forming surfactant, can have a beneficial effect on the P-3CR, leading to a substantial increase in reaction yield.16 Surfactant aggregates like vesicles or micelles enable to overcome the main disadvantage of water as a solvent, namely the low solubility of organic compounds. In addition, the presence of surfactant aggregates may even enhance reaction rates.17 Therefore, the combination of the P-3CR with aqueous surfactant aggregates appears a valuable approach towards the development of an ideal, environmentally friendly synthesis. Furthermore, vesicle systems,18 may well be suited for further combining the P-3CR with enzymatic transformations.
Aldehydes (as carbonyl compounds) are typical starting materials of the P-3CR, although they may be unstable during storage, leading to the formation of the corresponding alcohols and other impurities.19 Moreover, the synthesis of aldehydes through oxidation of alcohols or reduction of carboxylic acids may be difficult since the reactions may not be selective and they may result in overoxidations or overreductions. One of the methods used to overcome this drawback is generating aldehydes in situ, in the reaction mixture,20 particularly as a first step of a reaction cascade (reduction of waste, which is generated during the isolation and purification of intermediates).21
In this context it was reported in the literature about a P-3CR with primary alcohols using o-iodoxybenzoic acid (IBX) as an oxidant,22 which is a potentially shock-sensitive explosive substance.23 Furthermore, there were reports on oxidations with pure oxygen combined with the P-3CR, using the CuCl2/TEMPO/NaNO2 system24 or a MNST (magnetic core–shell nanoparticles supported TEMPO)/TBN system,25 in both cases with toluene as solvent.
Unfortunately, all the mentioned methods for the oxidation of alcohols20 require hazardous reactants and toxic and expensive transition metals. Due to this fact, the products require tedious and expensive purification procedures, what make them unattractive for the pharmaceutical and cosmetic industries.26 Especially since in the pharmaceutical industry, for which the pharmacopoeia limits of heavy metal contaminations are below 5 ppm, most of the classical chemical methods with metal catalysts are unacceptable.
In order to fulfill the requirements mentioned above, we report about a new chemoenzymatic protocol based on a one-pot oxidation–P-3CR procedure. The oxidation of a primary alcohol to the corresponding aldehyde is conducted enzymatically by oxygen from air (without usage of O2, which can be potentially explosive), with the enzyme laccase and the mediator TEMPO. A schematic representation of this laccase/TEMPO system is shown in Scheme 1. After the oxidation, a carboxylic acid and an isocyanide are added, which initiate a P-3CR in the same “pot”, providing an α-acyloxy carboxamide. All reactions proceed in an aqueous surfactant system, which excludes the use of organic solvents like toluene, and reactants like NaNO2 and IBX, which are toxic, corrosive (IBX) and hazardous for the aquatic environment (NaNO2).27 Since, however, TEMPO and the surfactant are not fully renewable and appear as waste, the environmental (E) factor28 is lower than in a surfactant-free system. Therefore, we also investigated the reusability of the catalytic system.
As components for a model Passerini reaction, benzaldehyde (2a), benzoic acid (3a) and p-methoxybenzyl isocyanide (4a) were arbitrary selected. As shown before,16 if the reaction is performed in phosphate buffer in the presence of 20 mol% DODAB, 2-(4-methoxybenzylamino)-2-oxo-1-phenylethyl benzoate 5a is obtained with 92% yield. With these results in mind, we performed the reaction of 1a, 3a and 4a in the presence of laccase, TEMPO and DODAB in phosphate buffer (pH = 5.7). Moreover, we investigated the influence of the enzyme, the mediator, and the reaction time on the reaction yield. We also performed the reaction with 4-hydroxy-1H-benzotriazole (HOBt) instead of TEMPO as a mediator and we optimized the reaction time. The results are summarized in Table 1.
Entry | Mediator | Time (h) | Yield (%) |
---|---|---|---|
a Reaction conditions: benzyl alcohol (1a, 0.5 mmol), benzoic acid (3a, 0.5 mmol), p-methoxybenzyl isocyanide (4a, 0.5 mmol), mediator (0.1 mmol), laccase from Trametes versicolor (20 mg), DODAB (0.1 mmol) were stirred at room temperature in phosphate buffer (5 mL, pH = 5.7).b Estimated by TLC, absence of spot of the product (5a), 1a still clearly present in the reaction mixture.c Reaction carried out without enzyme.d Reaction carried out without DODAB.e Reaction performed without benzoic acid (3a), with 1 mmol of benzyl alcohol (1a). | |||
1 | TEMPO | 48 | <5b,c |
2 | — | 48 | <5b |
3 | TEMPO | 48 | 27d |
4 | TEMPO | 48 | <5b,e |
5 | HOBt | 48 | <5b |
6 | TEMPO | 24 | 47 |
7 | TEMPO | 48 | 64 |
8 | TEMPO | 72 | 64 |
The obtained results clearly prove, that the laccase/TEMPO system is crucial for the oxidation of benzyl alcohol (1a) to benzaldehyde (2a) (entries 1 and 2). If one of the two components was absent, the reaction did not take place. Comparison of entry 3 with entry 7 shows, that the presence of DODAB significantly increased the yield of 5a from 27% to 64%. The observed improvement of the reaction yield may be caused by the increase of the solubility of the reacting molecules in the hydrophobic part of the vesicular aggregates as well as by electrostatic attractions between the cationic surface of the vesicles and the benzoic acid anions. Analysis of the reaction conducted without 3a (entry 4) showed that overoxidation of 1a to 3a did not occur. Furthermore, without laccase there was no aerobic oxidation of 2a (entry 1), which according to literature takes place, when pure water is used as reaction medium.29 For the conditions of entry 5, i.e. for the use of HOBt instead of TEMPO, no reaction took place, what proves that TEMPO is an efficient and ideal mediator in this type of biocatalytic oxidation reactions. Entries 6–8 show that 48 hours is an optimal time for this reaction, after 24 hours the yield of 5a was 47% and finally raised to 64%. Further reaction time prolongation did not impact the reaction yield.
Next, we focused on the optimizing of the buffer pH value. It is well recognized that enzymes are stable and active in a relatively narrow pH range. According to literature, laccase from Trametes versicolor is active in the pH range from 3 to 6.30 We performed reactions of 1a, 3a and 4a in the presence of laccase, TEMPO and DODAB in phosphate buffers in the pH range between 3 and 8. Appropriate buffers were prepared by mixing 0.1 M solutions of orthophosphoric acid, sodium dihydrogen phosphate and disodium hydrogen phosphate to adjust the pH to the desired value. In the optimal range of pH, between 5 and 6, additional experiments were performed. All results are shown in Fig. 1.
Although the optimal pH for the model laccase/TEMPO oxidation–P-3CR system was found to be 5.2, in the range from pH = 5 to 6 the yield of 5a varied only slightly. Decreasing the pH value below 5, the yield of 5a dropped, probably due to the acid catalyzed hydrolysis of the isocyanide.31 At pH > 6, the yield of 5a also dropped, which is probably due to a decrease in laccase activity.30
In a next step of our investigations, we focused on a variation of the surfactant type. From our previous studies we already know, that DODAB was the best among the surfactants and other additives tested for performing the Passerini reaction in aqueous systems.16 Afterwards, we checked whether DODAB is also the most suitable surfactant for the enzymatic transformation of 1a to 2a, preceding by the Passerini reaction. To investigate this point, we performed reactions of 1a, 3a and 4a in the presence of laccase, TEMPO and different additives (20 mol%). The formation of 5a was analyzed (Table 2).
Entry | Additive (20 mol%) | Yield (%) |
---|---|---|
a Reaction conditions: benzyl alcohol (1a, 0.5 mmol), benzoic acid (3a, 0.5 mmol) and p-methoxybenzyl isocyanide (4a, 0.5 mmol), TEMPO (0.1 mmol), laccase (20 mg), DODAB (0.1 mmol) in 5 mL of phosphate buffer (pH = 5.2, c = 0.1 M) for 48 h at room temperature. | ||
1 | — | 21 |
2 | Montmorillonite K 10 (10 mg) | 16 |
3 | Sodium dodecyl sulphate (SDS) | 6 |
4 | Sodium bis(2-ethylhexyl)sulfosuccinate (AOT) | 12 |
5 | Cholesterol | 22 |
6 | Tween 80 | 23 |
7 | Triton X-100 | 47 |
8 | 3-(N,N-Dimethylmyristylammonio)propanesulfonate | 23 |
9 | Didodecyldimethylammonium bromide | 34 |
10 | Dioctadecyldimethylammonium bromide (DODAB) | 67 |
For the reaction performed without any additive, 5a was obtained with 21% isolated yield. Addition of montmorillonite K 10 (entry 2) resulted in a decrease of the yield to 16%. Entries 3 and 4 show, that the addition of anionic surfactants (SDS or AOT) caused a significant decrease in reaction yield, probably due to repulsive interactions between the benzoic acid anions (deprotonated form of 3a) and the negatively charged surface of the micellar or vesicular aggregates formed. Addition of cholesterol (entry 5) had a negligible effect, similarly to the addition of the non-ionic surfactant Tween 80 (entry 6) or the zwitterionic surfactant 3-(N,N-dimethylmyristylammonio)propanesulfonate. In all these cases, the reaction yields were almost the same as without additive. In the presence of the non-ionic surfactant Triton X-100, the reaction yield was significantly increased, probably due to a positive effect of this neutral surfactant on the P-3CR, associated with an increased solubility of the reactants in the reaction medium. Addition of the two different cationic surfactants with the long aliphatic side chains; didodecyldimethylammonium bromide or DODAB (entries 9 and 10) enhanced the yield of 5a. The best result was obtained in the presence of DODAB, which is known to form bilayers in aqueous solutions, present as dispersed vesicles,32 the reaction yield was increased from 21% without any additive (entry 1) to 67% (entry 10). This indicates that DODAB is the most suitable additive among the ones checked for the Passerini reaction preceded by the laccase-catalyzed oxidation.
Next, the reaction was studied by varying the DODAB concentration, ranging from 5 to 50 mol%. For each condition, the critical concentration for aggregate formation (cac) was reached (for H2O, 25 °C, cac(DODAB) = 4.28 × 10−5 M).33 The results are shown in Fig. 2. In the presence of 5 mol% DODAB the reaction yield remained comparable to the one without surfactant. Upon increasing the amount of DODAB from 5 to 20 mol%, the yield of 5a increased up to 67%. A further elevation of the DODAB concentration from 20 to 50 mol%, did not improve the yield further. Based on these data, DODAB was used at a concentration of 20 mol% for all further experiments as optimal concentration.
In order to try to improve the reaction yield to a level which is close to the yield of the enzyme-free reaction carried out with 2a, 3a and 4a (92%),16 we performed a few experiments in which the amount of benzyl alcohol (1a) as one of the starting materials was changed. Usage of 2 equivalents of 1a resulted in product 5a with 76% yield, and with 5 equivalents the yield of 5a was 79%. For a reaction carried out with 2 equivalents of isocyanide (3a) resulted in 5a with 88% yield. These experiments indicate that very high yields cannot be achieved with the laccase/TEMPO–P-3CR system due to the possible accompanying hydrolysis of 3a. In order to overcome this problem the reaction was conducted stepwise: first 24 hours oxidation of 1a with laccase, TEMPO and surfactant, followed by the Passerini reaction with 3a and 4a for another 24 hours, resulting in product 5a with 86% yield (Table 3, entry 1).
Entry | Recycle | Yield (%) |
---|---|---|
a Reaction conditions: 1a (0.5 mmol), TEMPO (initially 0.1 mmol), laccase (initially 20 mg), DODAB (initially 0.1 mmol) in 5 mL of phosphate buffer (pH = 5.2, c = 0.1 M) were mixed for 24 h at room temperature, then 3a (0.5 mmol) and 4a (0.5 mmol) were added and the reaction mixture was stirred for additional 24 h. | ||
1 | Fresh catalysts | 86 |
2 | I recycle | 67 |
3 | II recycle | 19 |
From an environmental point of view, the reusability of the catalytic system is a critical issue. Therefore, we investigated whether the catalytic system based on the laccase/TEMPO oxidation and the DODAB vesicular suspension can be used more than once. The model reaction was carried out according to the optimized procedure, benzyl alcohol (1a, 0.5 mmol), TEMPO (0.1 mmol), DODAB (0.1 mmol) in 5 mL of phosphate buffer (pH = 5.2, c = 0.1 M) were incubated with laccase (4 mg mL−1) for 24 h at room temperature, then benzoic acid (3a, 0.5 mmol) and p-methoxybenzyl isocyanide (4a, 0.5 mmol) were added and the reaction mixture was stirred for additional 24 h. During the progress of the reaction, solid product 5a formed and felt out in impure form from the reaction mixture. The product could be separated by filtration through a cotton pad, followed by purification using column chromatography. The filtrate containing DODAB, enzyme and TEMPO in phosphate buffer was employed for another run: 1a was added first, then – after 24 h – 3a and 4a were added, and the reaction was carried out for additional 24 h. After filtration through a cotton pad, the filtrate containing the surfactant, laccase and TEMPO was used for the reaction one more time. The results from these catalytic system reusability tests are shown in Table 3 (entries 2 and 3). The laccase/TEMPO and DODAB catalytic system could be reused one time with an appreciable decrease in yield from 86% (entry 1) to 67% (entry 2). Afterwards, there was a large drop in yield to 19% (entry 3). This decrease in reaction yield may be due to a deactivation of the enzyme with time and/or a significant loss in laccase, TEMPO or DODAB during the filtration step.
After the optimization of the reaction conditions for benzyl alcohol (C6H5–CH2OH, 1a), experiments with other alcohols (R–CH2OH, 1) were also carried out. Alcohol 1 was mixed with laccase, TEMPO and DODAB in phosphate buffer at room temperature, after 24 h 3a and 4a were added, and the isolated yields were determined after additional 24 h. The results are summarized in Table 4.
Entry | R | 5 | Yield (%) |
---|---|---|---|
a Reaction conditions: alcohol (1, 0.5 mmol), TEMPO (0.1 mmol), laccase (20 mg), DODAB (0.1 mmol) in 5 mL of phosphate buffer (pH = 5.2, c = 0.1 M) were mixed for 24 h at room temperature. Then benzoic acid (3a, 0.5 mmol) and p-methoxybenzyl isocyanide (4a, 0.5 mmol) were added and the reaction mixture was stirred for additional 24 h.b Mixture of diastereoisomers, dr = 1![]() ![]() |
|||
1 | C6H5 | 5a | 86 |
2 | p-NO2C6H4 | 5b | 78 |
3 | p-FC6H4 | 5c | 72 |
4 | p-ClC6H4 | 5d | 65 |
5 | p-MeC6H4 | 5e | 68 |
6 | p-OMeC6H4 | 5f | 62 |
7 | CH![]() |
— | 0 |
8 | C11H23 | 5g | 11 |
9 | CH(C2H5)C4H9 | 5h | 30b |
10 | CH![]() |
5i | 81 |
For the reactions carried out with derivatives of benzyl alcohol (entries 2–6), the resulting yields varied between 62 and 86%, with the highest one obtaining for benzyl alcohol (1a). These results indicate that there is only a slight influence of the type of substituent in the benzene ring on the reaction yield. In case of allyl alcohol (entry 7), no reaction occurred. This could be due to the highly reactive and polymerizable acrolein, which is the product of the oxidation reaction. This is probably the reason why – to the best of our knowledge – acrolein has never been used successfully as a substrate in P-3CR. Reactions carried out with alkyl alcohols, dodecanol (entry 8) and 2-ethylhexanol (entry 9) resulted in products 5g and 5h with 11% and 30% yields respectively, what corresponds to literature data for aliphatic alcohols oxidized by the laccase/TEMPO system.34 The reaction with the more demanding cinnamyl alcohol (entry 10) provided product 5i with 81% yield.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/c6ra13078j |
This journal is © The Royal Society of Chemistry 2016 |