Longfei
Wang‡
a,
Yuanyuan
Hu‡
ab,
Qingqing
Pu
a,
Yongqiang
Yao
a,
Hao
Zhang
a,
Yong
Guo
a,
Yongsheng
Li
*a,
Bin
Dai
a and
Zhengang
Ke
*a
aSchool of Chemistry and Chemical Engineering, State Key Laboratory Incubation Base for Green Processing of Chemical Engineering, Shihezi University, Shihezi, 832003, China. E-mail: ysli@ecust.edu.cn; zgke@shzu.edu.cn
bFirst Affiliated Hospital of Shihezi University, Shihezi, 832008, China
First published on 15th November 2024
N-Formamides are important high-value chemicals with a wide array of applications. Whilst the oxidative carbonylation of amines with paraformaldehyde is a green route to synthesize N-formamides, the reaction suffers from the drawback of having to use noble metal catalysts. Herein, a non-noble metal CoNC catalyst was developed for the oxidative carbonylation of amines with paraformaldehyde. A series of N-heterocycles, aliphatic amines and anilines with different substituents were suitable for reaction over this CoNC catalyst, and moderate to good yields of the N-formylated amines were obtained. A mechanistic investigation suggests that both singlet oxygen (1O2) and the superoxide anion (O2−) are the active oxygen species of the oxidative carbonylation reaction. Co-Nx single atom sites are the possible catalytic active sites on the CoNC catalyst.
Sustainability spotlightN-Formamides are important high-valuable chemicals with a wide array of applications. Whilst the oxidative carbonylation of amines with paraformaldehyde is a green and sustainability route to synthesize N-formamides, the reaction suffers the drawback of having to use noble metal catalysts. Catalysis using abundant metals is more in line with the concept of green sustainable development. Herein, a non-noble metal CoNC catalyst was developed for the oxidative carbonylation of amines with paraformaldehyde. |
N-Formamides are synthesized via the reaction of amines with carbonyl reagents such as CO, triethyl orthoformate, chloral, glyoxylic acid, and ethyl acetate. This reaction suffers from drawbacks such as toxic raw materials and low atom-economy.16–18 In recent years, a series of green N-formylation routes were developed,19–21 for example, the oxidative carbonylation of amines with methanol22–24 or formaldehyde,25–30 the dehydration condensation of amines with formic acid,14,31 and the reductive carbonylation of amines with CO2/H2 (ref. 32–37) (Scheme 1). The oxidative carbonylation of amines with formaldehyde is a fascinating route for the synthesis of N-formamides because the starting materials are widely available and water is the only by-product, and thus it can be performed under mild conditions which is favorable for the synthesis of drug molecules.38
Formaldehyde is conveniently obtained via the aerobic oxidation of renewable methanol39–41 over a silver catalyst.42,43 Since a pioneering work on the oxidative carbonylation of amines with formaldehyde over an iridium complex,26 a series of Au/PVP,25 Ag (110),27 Au/CNT,28 Au/Al2O3 (ref. 29) and Au/TiO2 (ref. 30) catalysts were developed for the reaction (Scheme 1 and Table S1, ESI†). Although the above catalysts are effective for the oxidative carbonylation of amines with formaldehyde, they suffer from the drawback of having to use noble metal catalysts which hamper their industrial applications.44 It is therefore imperative to develop non-noble metal catalysts for the oxidative carbonylation of amines with formaldehyde.19
Nitrogen-doped carbon supported metal (MNC) catalysts are considered to be a substitute for Pt-based catalysts in electrochemical oxygen reduction reactions.45–48 Because of its unique cation metal center and metal nitrogen coordination structure, MNC have attracted increasing interest for use in thermocatalytic reactions. For example, the oxidation of alcohols to carboxylic acids,49,50 the oxidative esterification of alcohols to esters,49,51 the ammoxidation of alcohols to nitriles or amides,49,50 and the oxidative dehydrogenation of N-heterocycles.52–54 However, the oxidative N-formylation of amines with formaldehyde over MNC catalysts remains undeveloped. Cobalt has a specific electronic structure, and it has been established as one of the most important non-noble metal catalysts in hydrogen transfer55 and aerobic oxidation reactions.50,56–59
Herein, a non-noble metal CoNC catalyst was developed via pyrolysis of the complex formed between a cobalt salt (e.g., CoCl2) and ligand (e.g., phenanthroline). The resulting catalyst allows for the oxidative carbonylation of N-heterocycles, aliphatic amines, and aromatic amines with paraformaldehyde under mild conditions. Free radical quenching experiments show that both singlet oxygen (1O2) and the superoxide anion (O2−) are the possible active oxygen species during the reaction with this CoNC catalyst.
CoCl2 and the complex of CoCl2 coordinated with 1,10-phenanthroline (1,10-Ph) show no activity for the reaction. CoNC-700-WA was synthesized via the same method without acid etching, however it showed negligible catalytic activity for the reaction (Fig. 1b). After acid etching, an excellent yield of 1b was obtained over CoNC-700, which indicated that metallic cobalt and cobalt oxide were not the active metal species. CoNC-700-NP was prepared via impregnation of CoCl2 on an XC-72R support and subsequence reduction with NaBH4, but 1b was not obtained under the same reaction conditions. The above results indicated that nano metallic cobalt and cobalt oxide were not the active metal species. CoNC-700-CoBr2 was synthesized via the same method using CoBr2 and 1,10-Ph as precursors, and the yield of 1b was 59%, suggesting that the anion of the cobalt salt plays an important role for the formation of the active CoNC catalyst. CoNC-700-ZIF-8 was synthesized via pyrolysis of the CoCl2-based ZIF-8, and the yield of 1b was 51%. This suggests that the unique structure of the CoNC-700 was the source of the activity for the carbonylation reaction.
According to previous reports, the pyrolysis temperature affects the electronic structure of MNC catalysts.61 Next, CoNC catalysts pyrolyzed at different temperatures (500, 600, 700, 800, 900, and 1000 °C) were synthesized to study the effects of the CoNC structure on the reaction. The yield of 1b was 24% when CoNC was pyrolyzed at 500 °C. Upon increasing the pyrolysis temperature, the yields of 1b were increased. The highest yield of 1b was obtained over CoNC-700. Increasing the pyrolysis temperature further resulted in a decrease in the yields of 1b, and the yield of 1b decreased to 20% over CoNC-1000 (Fig. 1c). The BET surface area of the CoNC catalysts at different pyrolysis temperatures was tested. The BET surface areas of CoNC-600, CoNC-700 and CoNC-800 were found to be 321, 528, and 345 m2 g−1 respectively, which suggests that a higher surface area is advantageous for the reaction (Table S2, ESI†). According to the XRD spectra, CoNC-700 shows the best dispersion, which is a possible reason for its high activity (Fig. 2a).
In the absence of a base additive, the yield of 1b was obviously decreased, which suggests that a base is necessary for the reaction to proceed (Fig. 1d). The yield of 1b was increased to 55% from 27% when 0.2 equiv. of KOH was added, probably because the base favors the depolymerization of paraformaldehyde. Na2CO3 and NaOH obviously improved the reaction outcome, and the highest yield of 1b was obtained when 0.2 equiv. of NaOH was added. The organic base tBuONa was tested, but it did not promote the reaction as well as the inorganic bases did, possibly because the organic base was unstable under the reaction conditions. The effect of the NaOH loading on the reaction was studied, and it was found that the yield of 1b decreased as the NaOH loading decreased.
CoNC-700 showed low activity in weak polarity n-heptane solvent, and the yield of 1b was only 41% (Fig. 1e). The yields of 1b were 35% and 34% in tetrahydrofuran (THF) and 1,4-dioxane, respectively, which suggests that an obvious solvent effect exists. The yield of 1b was obviously increased in γ-valerolactone, and the yield of 1b was 77%. According to previous reports, acetonitrile (CH3CN) is an excellent solvent for oxidation reactions.62 Consistent with reported results, CH3CN was the most effective solvent for the reaction, and the yield of 1b was increased up to 90%. The strong polar solvent N,N-dimethylformamide (DMF) was not suitable for the reaction, and the yield of 1b was only 23%. The effect of the oxygen pressure on the reaction was also investigated, and it was found that the yield of 1b was decreased to 50% when the oxygen pressure was decreased to 0.1 MPa.
The stability of the CoNC-700 catalyst was investigated. After the reaction, the reaction solution was analyzed using ICP-MS after removal of the CoNC-700 catalyst via centrifugation (13000 rpm). Only 0.0094 ppm cobalt was detected, which suggests that only a negligible quantity of cobalt from CoNC-700 was leached to the reaction solution. A hot filtration experiment was performed under the reaction conditions. After 6 h, the CoNC-700 catalyst was removed from the reaction system via hot filtration, the yield of 1b was 43%. Subsequently, the autoclave was sealed and charged with 0.5 MPa O2 and the reaction was continued for another 6 h, and the yield of 1b was not significantly changed at 40%. This suggests that none of the active catalytic species was present in the reaction solvent.
CoNC-700 was applied to oxidative carbonylation of various amines with paraformaldehyde, and the results are shown in Table 1. N-Heterocycles are an important active chemical in pharmaceutical synthesis. The CoNC-700 catalyst was effective for the oxidative carbonylation of N-heterocycles including morpholine, piperidine and N-methyl piperazine with paraformaldehyde, and 67–90% of the target products were obtained (Table 1, entries 1–3). Primary aliphatic amines were obtained via the reductive amination of ammonia with aliphatic aldehydes, which in turn were sourced from the hydroformylation of olefines.6 A 60% yield of N-octyl formamide was obtained via the reaction of n-octylamine with paraformaldehyde over CoNC-700 (Table 1, entry 4). The yield of N-hexyl-N-methyl formamide was 83% (Table 1, entry 5). Other secondary aliphatic amines such as N,N-dipropyl amine, N,N-dibutyl amine, and N,N-dihexyl amine showed excellent activity under the reaction conditions, and 68–79% target products yields were obtained, suggesting that secondary aliphatic amines showed better activity than primary aliphatic amines (Table 1, entries 6–8).
Entry | Substrates | Products | Yield (%) |
---|---|---|---|
a Reaction conditions: amine (0.5 mmol), paraformaldehyde (0.75 mmol), CoNC-700 (10 mg), NaOH (0.2 equiv.), O2 (0.5 MPa), CH3CN (2 mL), 60 °C, 12 h, isolated yields. b 120 °C, 24 h. c 140 °C, 12 h. | |||
1 |
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90 |
2 |
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67b |
3 |
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74b |
4 |
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60b |
5 |
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83c |
6 |
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78c |
7 |
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68c |
8 |
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79c |
9 |
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72b |
10 |
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85b |
11 |
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74b |
12 |
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66b |
13 |
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50c |
14 |
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50c |
The oxidative carbonylation of aniline proceeded smoothly, and 72% yield of N-formyl aniline was obtained (Table 1, entry 9). Next, the effect of the functional groups on the aniline benzene ring was investigated. An aniline with an electron-donating methyl group showed excellent activity, and 85% yield of 4-methyl N-formyl aniline was obtained (Table 1, entry 10). This suggests that the electron-donating methyl substituent was favoured by the reaction. Halogen-substituted anilines were tested and 4-fluoro aniline, and 4-chloro aniline were also found to be suitable for the reaction, but slightly decreased yields of the target products obtained (Table 1, entries 11 and 12). This indicates that a halogen substituent on the benzene ring of the aniline is unfavoured by the reaction, and the negative effect increased with an increase of the atomic radius of the halogen atoms. An aniline derivative possessing a strong electron-withdrawing trifluoromethyl group, could also be oxidatively carbonylated, and the yield of 4-trifluoromethyl formyl aniline was 50% (Table 1, entry 13). A secondary aromatic amine, N-methylaniline, was reacted over CoNC-700, and 50% yield of the N-formylated product was obtained (Table 1, entry 14).
To investigate the mechanism of the oxidative reaction, a series of control experiments were performed (Scheme 2). The yield of 1b decreased to 32% from 90% in the presence of 1.0 equiv. of NaN3, which suggests that singlet oxygen (1O2) is the active oxygen species. When p-benzoquinone (PBQ2) was added, only 17% 1b was obtained, indicating that superoxide anion (O2−) was also an active oxygen species. The yield of 1b was 16% in the presence of PBQ2 and NaN3, further indicating that 1O2 and O2− were the active oxygen species.
To reveal the relationship between the activity and structure of the catalyst, the prepared catalysts were characterized. As depicted in Fig. 2a, the XRD pattern of CoNC-700 showed only characteristic carbon peaks and no diffraction peaks in relation to Co species, indicating that the Co atoms were highly dispersed on the N-doped carbon. However, obvious diffraction peaks were observed when CoNC was formed by pyrolysis at other temperatures, which suggests that amorphous carbon is beneficial for the reaction. According to the above analysis (Fig. 1a), the cobalt was the active material of this CoNC catalyst. The BET surface area of the CoNC-700 catalyst was 528 m2 g−1, which is beneficial for the formation of highly dispersed cobalt active sites.63 N2 adsorption–desorption isotherms exhibited typical type IV curves, along with an H1 hysteresis loop, suggesting the formation of a mesoporous structure which is favourable for the diffusion of reactants and products (Fig. S2, ESI†).
ICP-AES showed that the Co metal content in CoNC-700 was 2.45 wt%. X-ray photoelectron spectroscopy (XPS) was carried out to determine the surface electronic information relating to CoNC-700 (Fig. 2b–d and S3, S4, ESI†). The surface concentration of cobalt determined by XPS is 0.81 at%, which is negligibly higher than the ICP-AES result. This indicated that the cobalt was uniformly distributed on surface and in the body of CoNC-700. The characteristic peak of the Co 2p3/2 spectrum of CoNC-700 was mainly located at 780.78 eV, suggesting the presence of Co-Nx species (Fig. 2b).64,65 The N 1s spectrum displays the presence of four nitrogen species, pyridinic-N (398.4 eV), Co-Nx (399.0 eV), pyrrolic-N (400.0 eV), and graphitic-N (401.0 eV) (Fig. 2c).66,67 Two peaks at 531.84 and 533.14 eV were observed in the O 1s spectrum (Fig. 2d), which suggests that CO and H–O–C species exist on the surface of CoNC-700.68,69
To further identify the structure of the CoNC-700 catalyst, X-ray absorption fine structure (XAFS) spectroscopy was performed. The energy of the absorption edge of CoNC-700 was between cobalt phthalocyanin (CoPc) and CoO (Fig. 2e), indicating that the chemical state of the Co species was +2. From the Fourier-transform (FT) EXAFS analysis of CoNC-700, the first shell exhibits an obvious FT peak at 1.42 Å attributed to the CoNx coordination.66 Only this single peak appears in each FT-EXAFS spectrum of CoNC-700, which means that only Co single atom species are present in CoNC-700 (Fig. 2f). Therefore, CoNx single atom sites are the possible catalytic active sites of the CoNC-700 catalyst.
A possible reaction mechanism of this CoNC-700-catalyzed oxidative carbonylation of 1a with paraformaldehyde is proposed (Fig. 3). Firstly, paraformaldehyde was dissociated to formaldehyde in the presence of NaOH. Subsequently, molecular oxygen was converted to the active 1O2 and O2− oxygen species over the CoNC-700 catalyst. At the same time, morpholino methanol was formed via coupling of 1a with formaldehyde. Finally, the morpholino methanol was oxidatively dehydrogenated to 1b by the active 1O2 and O2− oxygen species over the CoNC-700 catalyst.
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Fig. 3 The possible reaction mechanism of the oxidative carbonylation of 1a with paraformaldehyde over the CoNC-700 catalyst. |
Footnotes |
† Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d4su00591k |
‡ These authors contributed equally to this work. |
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