Bruce A.
Lobo Sacchelli
ab,
Ruben S. M.
Almeida
a,
Abdallah G.
Mahmoud
a,
Dmytro S.
Nesterov
a,
Leandro H.
Andrade
b,
Ana M. M.
Faisca Phillips
*a,
Elisabete C. B. A.
Alegria
*ac and
Martin H. G.
Prechtl
*ad
aCentro de Química Estrutural, Instituto Superior Técnico, Universidade de Lisboa, Av. Rovisco Pais 1, 1049-001, Lisboa, Portugal. E-mail: ana.faiscaphillips@tecnico.ulisboa.pt; martin.prechtl@tecnico.ulisboa.pt; Web: https://cqe.tecnico.ulisboa.pt Web: http://www.h2.bio
bDepartamento de Química Fundamental, Instituto de Química, Universidade de São Paulo, Av. Prof. Lineu Prestes, 748 – Butantã, São Paulo – SP 05508-900, Brazil
cDepartamento de Engenharia Química, Instituto Superior de Engenharia de Lisboa, Instituto Politécnico de Lisboa, 1959-007 Lisboa, Portugal. E-mail: elisabete.alegria@isel.pt
dDepartment of Synthesis and Analysis, Albert-Hofmann-Institute for Physiochemical Sustainability, Albert-Schweitzer-Str. 22, 32602 Vlotho, Germany Web: https://www.a-h.institute
First published on 23rd January 2024
Herein we report on the catalytic oxidation of amines to nitriles with either pure oxygen or nitrous oxide, using the air- and water-stable organometallic complex {[(p-cymene)Ru](μ-H)(μ-Cl)(μ-HCO2)[Ru(p-cymene)]}BF4 which has been previously reported to be active for a series of biomimetic transformations, including formaldehyde dehydrogenase and dismutase, and transfer-hydrogenation reactions like deamination of nitriles to alcohols. Inline with these previous studies we now report on other biomimetic properties of this binuclear ruthenium complex which is able to act as well as nitrous oxide reductase (N2OR) and decompose nitrous oxide in the presence of hydrogen donating molecules like amines and alcohols. This complex can be synthesised from the inexpensive and commercially available precursor [Ru(p-cymene)Cl2]2 or from ruthenium chloride and renewable α-phellandrene which naturally occurs in eucalyptus oil for example. The selectivities and yields can be controlled by solvents, oxidants and temperature. Albeit oxygen is known as a potent oxidant, the observation that the catalyst can both oxidise alcohols or amines and simultaneously decompose the greenhouse gas nitrous oxide is very interesting. In addition, under similar conditions this catalyst is able to convert aromatic alcohols to benzaldehydes. These reactions with an air stable and robust catalyst were easy to carry out and affordable, making them highly practical. Note, in here we report on the oxidation of benzylamines and benzylic alcohols as model substrates for the initial evaluation of these catalytic set-ups.
Fig. 1 Biological and biomimetic oxidation of C–O and C–N bonds.1,2,7,8,18,29 |
Both benzonitriles and benzaldehydes have a wide range of applications, for a broad variety of industries. For example benzonitriles are used in pesticides since the 1970's,26 in the synthesis of benzoguanamine resins,27 or for the synthesis of fluvoxamine, an important antidepressant, that uses 4-(trifluoromethyl)benzonitrile as a key intermediate,28 one of the compounds that we also prepared in this work.
Industrially, nitriles are typically synthesized by ammoxidation, a high-temperature vapor-phase oxidation process involving toluene and ammonia. This occurs in fixed-bed reactors operating at temperatures between 300 and 550 °C, with catalysts ranging from vanadium and molybdenum, to a tungsten–manganese complex.27,30,31 Classically, on a laboratory scale, benzonitriles are conventionally prepared through two main reactions: the Rosenmund–von-Braun reaction from aryl halides at 150–250 °C using Cu(I) cyanide as a cyanating agent,32,33 or the Sandmeyer reaction, starting from benzylamines through diazotization, also using copper cyanide.34 This latter one, is also used in industrial scale to produce antipsychotic drug Fluanxol and the anti-cancer drug neoamphimedine.35,36 Benzaldehydes also play an important role in the industry. For instance, benzaldehyde is the simplest and most important aromatic aldehyde in industry.37,38 It is known for its bitter almond odour and taste, and it is only behind vanillin as the most used flavouring agent, it is also commonly used as a denaturant and as a fragrance, in the cosmetic industry.39 Its industrial process is based on the hydrolysis of benzal chloride, usually using metal salts as catalysts, preferably those of iron or zinc, and could be carried out either continuously or in batch. More recently, the process has been adapted to work continuously with activated carbon as catalyst, resulting In yields over 97%, and can be used for the synthesis of substituted benzaldehydes.37 The aerial oxidation of toluene is another option, but requires very high temperatures and low yields due to the formation of secondary products.38 On the lab scale, benzaldehydes can be produced from a wide range of compounds, most commonly following a similar path to the industrial one, from benzyl chloride or toluene, or being extracted from natural sources, like cinnamon oil.40 Protocols by Yamada,41 Severin,42 Grützmacher43 and their co-workers for lab scale experimentation report on the oxidation of benzylic alcohols,41,42 and also light weight aliphatic alcohols43 using ruthenium complex catalysts and nitrous oxide as terminal oxidant, at elevated temperatures (100–150 °C) with moderate to good yields,41,42 and also very promising high activity at lower temperature (65–80 °C) for the oxidation of light weight aliphatic alcohols with the target to simultaneously reduce nitrous oxide.43
In more recent years, in the field of homogeneous catalysis, Szymczack et al. reported on aceptorless and oxidant-free conditions at 110 °C for the amine to nitrile conversion with moderate yields (17–75%), using a ruthenium hydride NNN-pincer complex further stabilised with two triphenylphosphine. Albeit the acceptorless and oxidant free conditions, the requirement of inert conditions limits the practical application and scalability.44 Another example with a ruthenium NNN-pincer complex has been demonstrated by Bera et al. reporting activity at 70 °C with catalyst loadings as low as 2 mol%.45 Moreover, Achard et al. demonstrated that commercially available [Ru(p-cymene)Cl2]2 catalyses this reaction as well under acceptorless/oxidant-free and inert conditions in dichlorobenzene at 110 °C with moderate yields (23–65%).46 Following this approach, it has been demonstrated by Kannan and Muthaiah that the catalyst performance under inert conditions could be further improved by the addition of hexamethylenetetramine as hydride source to activate [Ru(benzene)Cl2]2 and [Ru(p-cymene)Cl2]2 for the acceptorless dehydrogenation of amines to nitriles with good yields (71–91%).47–49 Other protocols on amine oxidation to nitriles were published by Parvulescu,50 Albrecht51 and their co-workers. The latter group reported their evaluation on the ruthenium catalysed conversion of 4-methylbenzylamine (0.2 mmol) to the corresponding nitrile under oxygen in presence of gaseous ammonia showing good yields for nitrile (85%), but rather high catalyst loadings and temperature (catalyst: 5 mol%, 150 °C). Impressively, Parvulescu50 reported a highly selective (>99 °C) oxidation of amines (0.14 mol) to nitriles at low-temperature (60 °C), but with the requirement of elevated pressure of oxygen (5 bar) or air (25 bar) and relatively high molecular catalyst loadings (ratio: 0.14 mmol amine vs. 0.01 mmol complex; 7 mol%). In a different approach, with a zirconia supported ruthenium catalyst and a strong base the selectivity for imines or nitriles could be controlled.52
Taking into account the above described limitations and our previous demonstrations with bench stable biomimetic catalysts, an appropriate air-stable complex should be capable to catalyse the reaction cascade from amine to nitrile under oxidative conditions without the requirement of inert conditions which will be discussed in more detail below.
Note, in here we report on the oxidation of benzylamines and benzylic alcohols as model substrates for the initial evaluation of these catalytic set-ups with nitrous oxide and oxygen. For the catalytic activation of aliphatic substrates improved modification of the reaction conditions are still required. Additionally we tested also air instead of pure oxygen, but observed lower conversions owing to the lower oxygen content in air which underlined also the requirement of higher concentrations of the respective oxidant in comparison to oxidant-free (inert) conditions. Moreover, for the development of a simplified setup we disregarded the addition of gaseous ammonia to improve the selectivity which is a typical workaround to shift the equilibrium in nitrile reduction and amine oxidation processes.51,53 Instead, since we demonstrated previously that this is also possible by the application of polar protic solvents in (de)hydrogenation processes, we continue to further develop our previous protocols in this field to influence the selectivity in such processes by means of polar-protic or non polar, non protic solvents.4,7,53–56
The oxidation of benzylamines is known to result in the formation of several by-products,44–49,52 mainly the respective secondary imine. Therefore further optimisation is required for improved reaction conditions avoiding inert conditions and water/air-sensitive catalysts. For this purpose, the benchmark substrate benzylamine was catalytically oxidised with O2 or N2O as terminal oxidant, in order to properly evaluate and investigate the effect of both these gases.
Thus, we verified the following parameters: (I) solvents, (II) oxidant (N2O vs. O2), (III) catalysts of interest (RuBF4vs. Ru2), (IV) reaction temperature, (V) reaction time, (VI) and (VI) reaction vessel (flask with gas balloon vs. sealed system (high vacuum tube with Teflon valve)). Notably, in systems equipped with balloons as gas reservoirs we avoided higher reaction temperatures owing to the observed potential boil off of the low boiling solvent and the related experimental errors towards reproducibility. The results (Table 1 and ESI:† Table S1) highlight tert-butanol as the most suitable solvent. In this solvent, we achieved the conversion of (>99%) benzylamine (1a) to benzonitrile (2a) with the best selectivity (90%) towards the desired nitrile product. Neat benzylamine turned out to be less suitable, since the high concentration of substrate shifts the reaction towards secondary imine formation, resulting in a mixture of nitrile (2a) and imine (3a) in ratios of approx. 4:6 with little effect of the used oxidant (Table 1: entry 1–2 and ESI:† Table S1). In water (Table 1: entry 3–4 and ESI:† Table S1) the selectivity was similar (4:6 and 5:5) and probably related to the miscibility and local concentration of benzylamine in water. In tert-butanol (Table 1: entry 5–6 and ESI:† Table S1) selectivities for nitrile are ca. 90% independent of the used oxidant (balloon). The increased gas solubility in alcohols may contribute to accelerating the catalytic oxidation reaction for nitrile formation compared to reactions in water, which has lower gas solubility. Consequently, we continued the studies with tert-butanol as solvent for the catalytic oxidation of amines to nitriles. Therefore, similar to our previous studies on nitrile hydrogenation7,53,54 the use of protic solvents are beneficial to shift the equilibrium and obtain the primary amine, or in the present case the nitrile rather than the secondary imine which is formed through condensation of the primary imine in presence of the primary amine. In addition one need to consider the miscibility of the organic substrates with the solvents which has influence of the local concentration, thus tBuOH appears more appropriate than water, and of course under neat conditions the concentration of benzylamine is also higher which shifts the equilibrium towards the imine.
Entry | Solvent | t [h] | Oxidant | Conv. [%] | 2 (3)a [%] |
---|---|---|---|---|---|
Reaction conditions: benzylamine (1 mmol, except entry 1–2; 4.5 mmol), solvent (1 mL, except entry 1–2: no solvent added), 65 °C, time varying, [Ru] = {[(p-cymene)Ru](μ-H)(μ-Cl)(μ-HCO2)[Ru(p-cymene)]}BF4 (RuBF4, 0.01 mmol; 0.22 mol% for entry 1–2 and 1 mol% for entry 3–6), oxidant gas varying (balloon). Conversions and yields were determined by GC and GC-MS analysis with hexadecane as internal standard. Imine quantities and benzylamine conversions were determined by 1H NMR analysis with cyclohexane as internal standard.a Nitrile 2 yield, the major side-product is the secondary imine 3 (yield in brackets). | |||||
1 | Neat | 70 | O2 | >99 | 40 (60) |
2 | N2O | >99 | 43 (57) | ||
3 | H2O | 70 | O2 | >99 | 41 (59) |
4 | N2O | >99 | 50 (50) | ||
5 | tBuOH | 70 | O 2 | >99 | 91 (9) |
6 | N 2 O | >99 | 89 (11) |
Subsequently, we investigated whether the commercially available [Ru(p-cymene)Cl2]2 (Ru2) could serve as a competitive alternative to RuBF4, under identical conditions (T = 35 °C or 65 °C, 20 h) using tert-butanol as solvent and balloons as reservoirs for the oxidants (Table 2 and ESI:† Table S1). It was observed that, under identical conditions, RuBF4 yielded better results. As a result we continued the studies with this complex. Interestingly, the comparison of reaction times (Table 1 entries 5–6 and Table 2 entries 7–10) suggests that selectivity is time-dependent. The secondary imine is not merely a by-product but a reaction intermediate formed in equilibrium. As soon as free primary imine is formed in equilibrium, the reaction shifts to nitrile formation under oxidative conditions.
Entry | Cat. | T [°C] | Oxidant | Conv. [%] | 2 (3)b [%] |
---|---|---|---|---|---|
Reaction conditions: benzylamine (1 mmol), tert-butanol (1 mL), 20 h, [Ru] = {[(p-cymene)Ru](μ-H)(μ-Cl)(μ-HCO2)[Ru(p-cymene)]}BF4 (1 mol%; 0.01 mmol) or [Ru(p-cymene)Cl2]2 (1 mol%; 0.01 mmol), oxidant gas varying (balloon). Conversions and yields were determined by GC and GC-MS analysis with hexadecane as internal standard. Imine quantities and benzylamine conversions were determined by 1H NMR analysis with cyclohexane as internal standard.a Reaction time: 24 hours.b Nitrile 2 yield, the major side-product is the secondary imine 3 (yield in brackets). | |||||
1 | Ru2 | 35 | O2 | 10 | 6 (94) |
2 | N2O | 6 | 0 (99) | ||
3 | Ru2 | 65 | O2 | 20 | 55 (45) |
4 | N2O | 10 | 30 (70) | ||
5 | RuBF4 | 35 | O2 | 17 | 55 (45) |
6 | N2O | 10 | 42 (58) | ||
7 | RuBF4 | 65 | O2 | >99 | 71 (29) |
8 | N2O | >99 | 67 (33) | ||
9 | RuBF4 | 65 | O2 | >99 | 85 (15)a |
10 | N2O | >99 | 77 (23)a |
Following the previous observations, we extended our exploration to optimise conversion and selectivities by adjusting the reaction time (4–70 h; Table 3) using RuBF4 as catalyst for the amine oxidation at 65 °C in tert-butanol. The time screening shows that >99% conversion can be reached after 16 h while the selectivity for nitrile is still about 70% (Table 3, entries 6–7). Longer reaction times further improved the selectivity (Table 3, 77–91%), while the results with oxygen are slightly better, but are not significantly more selective. Remarkably, this process offered the simultaneous decomposition and elimination of the greenhouse gas nitrous oxide.
Entry | t [h] | Oxidant | Conv. [%] | 2 (3)a [%] |
---|---|---|---|---|
Reaction conditions: benzylamine (1 mmol), tert-butanol (1 mL), [Ru] = {[(p-cymene)Ru](μ-H)(μ-Cl)(μ-HCO2)[Ru(p-cymene)]}BF4 (1 mol%; 0.01 mmol), oxidant gas varying (balloon). Conversions and yields were determined by GC and GC-MS analysis with hexadecane as internal standard. Imine quantities and benzylamine conversions were determined by 1H NMR analysis with cyclohexane as internal standard.a Nitrile 2 yield, the major side-product is the secondary imine 3 (yield in brackets). | ||||
1 | 4 | O2 | 26 | 67 (33) |
2 | N2O | 19 | 67 (33) | |
4 | 8 | O2 | 57 | 74 (26) |
5 | N2O | 21 | 67 (33) | |
6 | 16 | O2 | >99 | 70 (30) |
7 | N2O | >99 | 69 (31) | |
8 | 24 | O2 | >99 | 85 (15) |
9 | N2O | >99 | 77 (23) | |
10 | 70 | O2 | >99 | 91 (9) |
11 | N2O | >99 | 89 (11) |
To improve the reaction setup, we considered to substitute the balloon (used as an oxidant reservoir) and perform the reaction in a sealed reaction vessel (a gas-tight tube with a high vacuum Teflon valve) saturated with oxidant (Table 4). The idea is to have a better miscibility of the gaseous oxidants with the solute substrates and the catalyst, and the advantage that the temperature can be increased further. For this reason, we condensed 4.5 mmol nitrous oxide (at −196 °C) onto the reaction mixture and further optimised parameters such as time, temperature and solvent quantity (Table 4). Consequently, we were able to reduce the reaction time in this manner to achieve full conversion. However, the yields remained unchanged, which is most likely due to the considerable high concentration of the substrate and intermediate in solution, leading to the formation of the imine. Consequently, we tested then a more diluted reaction and doubled the amount of solvent (2 mL) and simultaneously varied the catalyst loading (0.5–2.0 mol%), shortened the reaction time further and increase of the reaction temperature to 95 °C, giving high conversions already in 12 h (Table 4, entry 11).
Entry | t [h] | [Ru] (mol%) | tBuOH [mL] | T [°C] | Conv. [%] | 2 (3)a [%] |
---|---|---|---|---|---|---|
Reaction conditions: benzylamine (1 mmol), tert-butanol (1 mL), [Ru] = {[(p-cymene)Ru](μ-H)(μ-Cl)(μ-HCO2)[Ru(p-cymene)]}BF4 (1 mol%, 0.01 mmol). Oxidant: nitrous oxide (4.5 mmol) condensed at −196 °C into the gas tight high vacuum tube with Teflon valve. Conversions and yields were determined by GC and GC-MS analysis with hexadecane as internal standard. Imine quantities and benzylamine conversions were determined by 1H NMR analysis with cyclohexane as internal standard.a Nitrile 2 yield, the major side-product is the secondary imine 3 (yield in brackets). | ||||||
1 | 2 | 1 | 1 | 65 | 25 | 43 (57) |
2 | 4 | 1 | 1 | 65 | 51 | 68 (32) |
3 | 4 | 0.5 | 1 | 65 | 37 | 59 (41) |
4 | 4 | 0.5 | 2 | 65 | 10 | 19 (81) |
5 | 4 | 2 | 1 | 95 | 59 | 38 (62) |
6 | 2 | 1 | 2 | 95 | 53 | 65 (35) |
7 | 4 | 1 | 2 | 95 | 69 | 67 (33) |
8 | 6 | 1 | 2 | 95 | 79 | 64 (36) |
9 | 8 | 1 | 2 | 95 | 87 | 70 (30) |
10 | 8 | 1 | 1 | 95 | 66 | 69 (31) |
11 | 12 | 1 | 2 | 95 | 97 | 70 (30) |
Now equipped with two distinct optimised reaction setups we conducted substrate scope screening with oxygen (balloon) with 1 mol% of RuBF4 as catalyst at 65 °C in tert-butanol (20 h; Table 5), and a second set with nitrous oxide (sealed flask) with 1.0 mol% of RuBF4 as catalyst at 95 °C for 12 hours (Table 4 and Table 6).
Entry | Benzylamine 1a–k/conv. [%] | Benzonitrile 2a–k/yield [%] | Imine 3a–k/yield [%] | Other byproducts of oxidation |
---|---|---|---|---|
Reaction conditions: 1 mol% (0.01 mmol) catalyst RuBF4, 1 mmol for all substrates, 1 mL tBuOH, 65 °C for 20 h. Oxidant gas O2 (balloon). Conversions, selectivity and yields were determined by GC and GC-MS analysis with hexadecane as internal standard. Imine quantities and benzylamine conversions were determined by 1H NMR analysis with cyclohexane as internal standard. n. q.: not quantified (traces).a Reaction time: 24 hours.b In [brackets]: isolated gravimetric yield after column chromatography (refer ESI† for details). | ||||
1 | Traces of benzamide and N-benzylidene benzamide | |||
>99 | 71 (85)a [71]b | 29 (15)a | ||
1a | 2a | 3a | ||
2 | — | Trace of benzamide | ||
>99 | >99 [89]b | |||
1b | 2b | |||
3 | Trace of benzamide | |||
>99 | 94 [72]b | 6 | ||
1c | 2c | 3c | ||
4 | Trace of 4-methyl benzamide | |||
>99 | 69 | 31 | ||
1d | 2d | 3d | ||
5 | Trace of 4-chloro benzamide | |||
>99 | 70 | 30 | ||
1e | 2e | 3e | ||
6 | Trace of 4-tertbutyl benzamide | |||
84 | 63 | 38 | ||
1f | 2f | 3f | ||
7 | Traces of benzamide and N-benzylidene benzamide | |||
72 | >98 | n. q. | ||
1g | 2g | 3g | ||
8 | Trace of 2-methoxy benzamide | |||
70 | 81 | 19 | ||
1h | 2h | 3h | ||
9 | Traces of benzamide and N-benzylidene benzamide | |||
53 | 41 | 59 | ||
1i | 2i | 3i | ||
10 | Trace of 2-chloro benzamide | |||
50 | 70 | 30 | ||
1j | 2j | 3j | ||
11 | Traces of benzamide and N-benzylidene benzamide | |||
39 | 94 | 6 | ||
1k | 2k | 3k |
With nitrous oxide as oxidant at 95 °C the conversions vary from 65 to >99% with selectivities for nitriles of 33 to 91%. The comparison of the results summarised in the Tables above one can conclude that both oxidants O2 and N2O are suitable for the benzylamine oxidation to benzonitriles with good conversions. However, lower temperature (65 °C) and longer reaction times (20 h) give better selectivities for nitriles than at higher temperature (95 °C) and shorter time (12 h).
Entry | BnOH/conv. [%] | PhCHO/yield [%] | Benzoic acid or benzyl benzoate/yield [%] |
---|---|---|---|
Reaction conditions: 2 mol% (0.01 mmol) catalyst RuBF4, 0.5 mmol for all substrates, 1 mL toluene, 95 °C for 16 h. Oxidant: oxygen (4.5 mmol) condensed at −196 °C into the gas tight high vacuum tube with Teflon valve. Conversions and yields were determined by GC and GC-MS analysis with hexadecane as internal standard and/or by 1H NMR analysis with cyclohexane as internal standard.a In (brackets): isolated gravimetric yield after column chromatography (refer ESI† for details). | |||
1 | — | ||
>99 | >99 (86)a | ||
4a | 5a | ||
2 | — | ||
>99 | >99 (92)a | ||
4b | 5b | ||
3 | — | ||
>99 | >99 (95)a | ||
4c | 5c | ||
4 | |||
>99 | 84 | 16 | |
4d | 5d | 7d | |
5 | |||
>99 | 82 | 18 | |
4e | 5e | 7e | |
6 | |||
>99 | 64 | 36 | |
4f | 5f | 6f | |
7 | |||
>99 | 48 | 52 | |
4g | 5g | 6g | |
8 | |||
>99 | 41 | 59 | |
4h | 5h | 6h | |
9 | — | ||
80 | >99 | ||
4i | 5i | ||
10 | — | ||
74 | >99 | ||
4j | 5j | ||
11 | — | ||
73 | >99 | ||
4k | 5k | ||
12 | — | ||
59 | >99 | ||
4l | 5l |
Footnote |
† Electronic supplementary information (ESI) available: Experimental and instrumental details on synthesis, catalysis and characterisation, including NMR, MS and GC data are available in the ESI. See DOI: https://doi.org/10.1039/d3cy01635h |
This journal is © The Royal Society of Chemistry 2024 |