Open Access Article
Bruno
Cerra
a,
Cecile
Blondeau
a,
Rolando
Cannalire
b,
Mariateresa
Giustiniano
b,
Shiva
Tali Shandiz
a and
Antimo
Gioiello
*a
aLaboratory of Medicinal and Advanced Synthetic Chemistry (Lab MASC), Department of Pharmaceutical Sciences, University of Perugia, Via del Liceo 1, Perugia, 06123, Italy. E-mail: antimo.gioiello@unipg.it
bDepartment of Pharmacy, University of Naples Federico II, Via D. Montesano 49, 80131, Napoli, Italy
First published on 29th November 2022
Isocyanides are valuable compounds for organic synthesis. However, the poor stability and distressing odour have often limited their widespread applications in common laboratory practice and industrial settings. Herein, a continuous flow approach to enable the synthesis, purification and in-line reaction of isocyanides is presented.
Isocyanides are produced industrially using phosgenation of alkyl or aromatic amines.3 However, the high toxicity of the gas raises safety concerns and requires special equipment. Other methods such as the Curtius rearrangement, and the Lieke–Meyer, Hoffmann, and Ugi reactions are generally employed in common laboratory practise.1,2 Although many other options exist, the vast majority of isocyanide syntheses still suffer from one or more issues including tedious protocols and work-up operations, expensive reagents, waste generation, and exposure to potentially hazardous fumes.
In the last few years, continuous flow chemistry has greatly facilitated the development of safe and efficient approaches for conducting forbidden chemical reactions.4 Adoption of flow synthesizers has been a determinant in moving towards green chemistry and more sustainable practices.5 In addition to improved process safety and quality, flow chemistry guarantees the fine-tuning of the reaction conditions, an efficient heat and mass transfer, and an extended operative window.6 Furthermore, the possibility to perform telescoped reactions and to integrate downstream operations avoids intermediate isolation, minimizing the exposure to toxic and hazardous reagents with a great improvement to the safety and environmental impacts.4 The merger of these benefits with automation promises to accelerate the development of new synthetic routes and compound throughput relieving expert chemists of routine tasks.7
In a previous work, Kim and colleagues reported the preparation of isocyanides in a microfluidic system with short reaction times and high yield.8a However, the method suffered from solubility and tube-plugging issues that were partially solved using ultrasound irradiation. In 2015, Baxendale and co-workers reported the telescoped flow synthesis of different heterocyclic building blocks, including 1,2,4-triazole and pyrrolo[1,2-c]pyrimidine scaffolds, using ethyl isocyanoacetate that was generated in situ by the dehydration reaction of N-formylglycine in the presence of triphosgene.8b
In this work, we present a streamlined method based on reactor technology for the serial synthesis, purification, scale-up and in-line reaction of isocyanides. Such an approach would solve major drawbacks, enable the progress and expand the scope of isocyanide chemistry.9 Combination with various reagents is conducted in a continuous fashion to provide diverse building blocks and important products without requiring the isolation of highly unstable and foul odour volatile isocyanides.
In order to set a benchmark with which our flow approach would be compared, we opted to conduct the Ugi synthesis of t-butyl isocyanide (1a) from the corresponding formamide 2a, in the presence of phosphorus oxychloride (POCl3) (1 equiv.) (Scheme 1A). Initially, diverse solvents (CHCl3, CH2Cl2, THF, 2-Me-THF) and organic bases (Et3N, DIPEA, pyridine, DIPA, TBA, DBU, DBN, proton sponge) were tested in batch modality to evaluate possible solubility issues and reactor clogging (data not shown). Most of the solvents and bases resulted in suspensions or in-line precipitation. Nevertheless, the desired t-butyl isocyanide (1a) was obtained in moderate to high yields. The best outcome was achieved with the use of CHCl3 and Et3N (5 equiv.) at 0 °C which ensured a clear solution (up to 0.6 M) and a high yield (82%). The aqueous work-up required careful hydrolysis to destroy the possible excess of POCl3, keeping basic pH conditions to avoid isocyanide decomposition. The crude isocyanide should be then purified, increasing the exposure to smelly odour over a rather long period.
Next, the reaction was repeated under flow conditions. As depicted in Scheme 1B, the flow set-up consisted of two syringe pumps to combine a solution of 2a (0.6 M solution in CHCl3) and Et3N with a stream of POCl3 (0.6 M solution in CHCl3) via a PEEK T-piece. A 20 mL PFA coil was used as the reactor, which was followed by a silica packed column for the in-line removal of salts and excess Et3N.9 In order to avoid aqueous work-up in favour of a simple alternative, the collected reaction mixture was analysed by quantitative 1H-NMR, using dimethyl sulfone as an internal standard. The procedure allowed a simpler set-up in addition to enabling rapid flow processing of materials and post-modification reactions. It was found that running the reaction for 20 min at 25 °C rendered the expected product 1a in excellent yield (89%) (Table 1, entry 1). A partial conversion (65%) was obtained by reducing the Et3N equiv. from 5 to 3. Using the best conditions, the reaction was proven effective in the multi-gram preparation of t-butyl isocyanide (1a) with a throughput of 3 mmol h−1 (Scheme 1B).
| Entry | Isocyanide | Yielda | Literature yield |
|---|---|---|---|
| Reactions were performed according to Scheme 1. (−) = No literature available from formamide to isocyanide via dehydration under standard conditions.a Yield determined by calibrated 1H-NMR analysis of the crude product in the presence of dimethyl sulfone as the internal standard.b DMSO (5%, v/v in CHCl3) was used as the co-solvent, [2g] = 0.15 M, [2i] = 0.36 M.c Isolated yield.d Conducted by reaction of 1a with POCl3 (1 equiv.) and of Et3N (5 equiv.) in CHCl3 at 0 °C until starting material consumption. | |||
| 1 |
1a
|
89% | 82%d |
| 2 |
1b
|
87% | 95%962%10 |
| 3 |
1c
|
79% | 67%10 |
| 4 |
1d
|
69% | (−) |
| 5 |
1e
|
Traces | (−) |
| 6 |
1f
|
87%11 | 91%12 |
| 7 |
1g
|
44%b,c | 93%9 |
| 8 |
1h
|
77% | 97%13 |
| 9 |
1i
|
79%b | 81%9 |
| 10 |
1j
|
80%c | 97%14 |
The method was applied to other N-substituted formamides 2b–j, and the formation of isocyanides was nearly completed within 20 min (Table 1). The criteria for substrate selection include the extensive usage, high volatility, foul odour, and toxicity of the resulting isocyanides.9 As a general trend, the reaction allowed the formation of the desired isocyanides with high purity and in good to high yields, except for formamides 2e and 2g (Table 1, entries 5 and 7). While allyl isocyanide 1e was formed in traces, the preparation of 2,6-dimethylphenyl isocyanide (1g) required the addition of 5% DMSO to ensure the complete solubility of the reaction mixture. Unfortunately, the use of DMSO caused the formation of solvent-derived by-products leading to a moderate reaction yield (44%) (Table S1, ESI†). In the case of aryl isocyanides, both electron-donating and -withdrawing groups work similarly well (entries 8 and 9). Comparison of our results with the ones reported in the literature under standard conditions has evidenced similar yields with a few exceptions; however, it should be pointed out that for these cases, the preparation required a long reaction time (24 h) and tedious protocols.
Having established a reliable flow method for the preparation and purification of pure isocyanides, our efforts were then focussed on the development of a flow system enabling in-line capture. The flow set-up has been designed to allow the serial synthesis of relevant scaffolds in medicinal chemistry (Scheme 2). The synthesizer was composed of a pump system, switching/mixing devices, two 10 mL coil reactors, back pressure regulators (BPRs), an autosampler, a UV detector, an automated flash chromatograph, and a fraction collector. Three sets of compounds, including 5-aminoimidazoles, 1,3-oxazoles, and β-amino amides such as the anaesthetic lidocaine, were prepared to showcase the feasibility of the flow system, using standard, non-optimized process conditions. At this stage, we aim to demonstrate the merging and compatibility of the reaction conditions and solvents between steps. This reaction scoping also served to assess the robustness of the processing conditions against the propensity for blockage formation.8 Notably, at the concentration studied for the flow set-up, no blockages occurred across the screened substrates and reactions. By not performing all steps simultaneously, the flow rates, concentrations, and temperatures can be easily adjusted without changing the equipment. Moreover, to permit reaction monitoring, and product detection and collection, an aliquot of the exit stream was analysed using a UV detector.
Footnote |
| † Electronic supplementary information (ESI) available: Details on experimental procedures, compound characterization and equipment are provided. See DOI: https://doi.org/10.1039/d2re00454b |
| This journal is © The Royal Society of Chemistry 2023 |