Sandeep
Kumawat†
a,
Sunidhi
Singh†
a,
Tarun
Bhatt
a,
Anjali
Maurya
a,
Sivakumar
Vaidyanathan
a,
Kishore
Natte
*a and
Rajenahally V.
Jagadeesh
*bc
aDepartment of Chemistry, Indian Institute of Technology Hyderabad, Kandi, Sangareddy 502 285, Telangana, India. E-mail: kishore.natte@chy.iith.ac.in; kishorenatte@gmail.com
bLeibniz-Institut für Katalyse e.V, Albert-Einstein-Straße 29A, Rostock 18059, Germany. E-mail: jagadeesh.rajenahally@catalysis.de
cNanotechnology Centre, Centre of Energy and Environmental Technologies, VŠB-Technical University of Ostrava, Ostrava-Poruba, Czech Republic
First published on 2nd February 2024
Production of value-added chemicals from renewable feedstocks is an attractive platform to alleviate the shortage of petroleum resources and to minimize CO2 emissions. Among different renewable feedstocks, glycerol is an organic triol molecule that is produced from triglycerides of plant and animal sources. This alcohol is produced as the main by-product in a large quantity of about 10% (w/w) in biodiesel production. In addition to its applications in food industries, and medicinal and personal care products, the utilization of glycerol as a key raw material in organic synthesis has garnered significant attention. As an example, selected technologies for the conversion of glycerol into other essential chemicals such as acrylic acid, 1,2-propanediol, glycerol carbonate, epichlorohydrin, and solketal have been well developed. In recent years, glycerol has also been used as the key starting material for the synthesis of amines in laboratories. In general amines are important fine and bulk chemicals used as central precursors and intermediates for advanced chemicals and many life science molecules including pharmaceuticals and agrochemicals. In the last five years, some key advancements have been made using glycerol in carbon–nitrogen bond-forming processes to prepare different kinds of amine in the presence of suitable catalytic systems. Based on the advantages of glycerol including its derived molecules as feedstocks and the importance of amines, we believe it is worthwhile to write a review summarizing the recent reports on glycerol amination and related reactions. In this regard, this review article discusses the latest developments in catalytic amination reactions using glycerol and its tangible applications in modern organic synthesis. We believe that this review will be interesting and beneficial to scientists working in the areas of catalytic utilization of glycerol aminations and valorization of renewable feedstocks.
Sunidhi Singh | Sunidhi Singh joined the Indian Institute of Technology Hyderabad as a research scholar in August 2022 and worked on organic fluorophores for OLED applications. |
Fig. 1 (A) Preparation of glycerol from the fossil-based route and bio-derived feedstock. (B) Glycerol market and applications. (C) Glycerol unit in pharmaceutical synthesis. |
Owing to the high presence of the hydroxyl (–OH) moiety in glycerol and its renewable nature, a variety of value-added chemicals can be manufactured from this alcohol, compared with petrochemical-derived feedstocks. Remarkably, glycerol also serves as a recyclable solvent in cross-coupling organic reactions.16 Thus, the valorization of glycerol is of prime importance in producing other products, which is an emerging research area in chemical synthesis.17–22 However, it should be noted that for achieving optimal efficiency, the purity of glycerol presents various challenges and also influences the reaction conversion as well as selectivity. The impurities (ash, non-glycerol organic matter, etc.) present in crude glycerol promote unwanted side reactions and impede the catalyst performance and overall reaction process.23 Despite these facts, over the past decade, noticeable research has been devoted to the use of glycerol in the synthesis and energy sectors, for example, in hydrogen generation, methanol production, as fuel additives including the production of bulk chemicals such as acrylic acid, 1,2-propanediol, glycerol carbonate, epichlorohydrin, and solketal and others.1–10,20,24–27 To valorize glycerol both chemical and biological processes such as dehydration, oxidation, hydrogenolysis, etherification, esterification, and amination processes have been applied.1–10 In the literature, it has been reported that glycerol dehydration mainly produces both acrolein and hydroxyacetone. Nevertheless, the selectivity of these products generally depends on the acid-based properties of the catalyst. Another important reaction is the carboxylation of glycerol, which gives glycerol carbonate in the presence of heterogeneous catalysts. This transformation represents many pathways and therefore makes this conversion more difficult.28 Next, the oxidation of glycerol can be conducted with any of the three hydroxyl units of the component. Many products (e.g., formic acid, glycolic acid, and glyceraldehyde) can be prepared by reacting glycerol with various oxidizing agents.28 The etherification of glycerol produces polyglycerols in the presence of solid catalysts. Interestingly, the use of acid catalysts leads to faster reactions as well as higher conversion, but very little selectivity. Conversely, by employing basic catalysts, the reaction will be slower, but with higher selectivity. Glycerol also reacts with oleic acid, acetic acid, or lauric acid and produces mono-, di-, and tri-glycerides in the presence of metal and mixed metal oxides.28 The hydrogenolysis of glycerol happens when any hydrogen source reacts with glycerol and typically produces a variety of products. Two of the most important ones are 1,3-propylene glycol and 1,4-propylene glycol.28 Nonetheless, all these aforementioned chemical routes typically lead to various side reactions and are not highly selective. In order to develop robust chemical processes starting from glycerol, developments must be achieved to increase conversion, selectivity, and yield under milder and environmentally friendly conditions. Based on these aspects, a number of research and review articles are published on the conversion of glycerol to value-added products.1–10,20
Among the synthetic applications of glycerol, its utilization as a feedstock to produce amines is of paramount importance because amines are highly privileged compounds, which serve as ever-required chemicals in academic laboratories and industries as well as life science activities.29,30 Since glycerol is the smallest polyhydroxylated compound, it could be easy to use as a model compound in theoretical and experimental investigations for the in-depth understanding of glycerol amination reactions under different catalytic reaction conditions. Apart from glycerol, bio-polyols like erythritol, xylitol, sorbitol, and mannitol have 4, 5, and 6 carbons and hydroxyl groups, respectively, which are also suitable for catalytic amination reactions.31 But the selective cleavage of carbon–carbon or carbon–oxygen bonds present in polyols is more challenging with respect to dehydrogenation, dehydration and other side reactions. Therefore, these bio-based feedstocks are less investigated than glycerol for catalytic amination reactions.
Typically, amines are produced by the hydrogenation of nitro compounds,32 hydrogenation of nitriles,33 reductive amination of carbonyl compounds,34 amination of alcohols/phenols,35 and hydroamination of olefins.36 In recent years, the use of polyols, particularly glycerol, has drawn significant attention in amination reactions to produce functionalized amines. As an example, a few potential pharmaceutical agents such as propranolol (β-blocker), indinavir (antiviral agent), and dropropizine (antitussive) comprise a glycerol unit, indicating the synthetic utility of glycerol as a potential building block in API synthesis (Fig. 1C).37–39 In recent years a lot of important efforts have been made on the catalytic amination of glycerol to prepare various amines by employing both homogeneous and heterogeneous catalysis.5,18,40–44 Despite interesting research articles on the amination of glycerol having been published, until now no related review has existed on the utilization of this alcohol for the synthesis of amines. Obviously, such a review article on the catalytic synthesis of amines involving glycerol as the feedstock will attract the attention of readers and researchers working in both academia and industry. Consequently, in this review, we comprehensively discuss these reports published in the last five years on the valorization of glycerol by catalytic aminations.
Ding and co-workers applied various types of heteropolyacid/Zr-MCM-41 catalytic system for the amination of glycerol with dimethylamine to produce dimethylamino-3-propanal.41 The authors found that H6P2W18O62/Zr-MCM-41 (Cat 2) displayed higher catalytic stability and selectivity than that of H3PW12O40/Zr-MCM-41 (Cat 1). The higher activity of Cat 2 is attributed to its higher surface area and pore volume as well as the fact it possesses more Brønsted acidic sites and a higher B/(B + L) ratio compared with Cat 1. Obviously, the presence of more Brønsted acid sites favoured the amination of glycerol.41 A plausible reaction pathway for the amination of glycerol (1) with dimethylamine (DMA) is shown in Scheme 2. The authors proposed two distinct dehydration pathways based on different types of acidic site. In the presence of Brønsted acid sites (Cat 2), glycerol dehydrogenates to 3-hydroxypropanal (7), which either can react directly with dimethylamine (DMA) to produce dimethylamino-3-propanal (9) or can easily convert to acrolein (8). The generated acrolein (8) subsequently reacts with dimethylamine (DMA) and results in the formation of dimethylamino-3-propanal (9). 3-Hydroxypropanal (7) can also be decomposed to formaldehyde (6) and acetaldehyde (4). On the Lewis acid sites, (Cat 1), the formation of hydroxyacetone (acetol, 2) takes place via the dehydration and deprotonation of the protonated intermediate. Next, hydroxyacetone (2) gets utilized in three pathways: the first one is the reaction of hydroxyacetone (2) with dimethylamine (DMA) to produce dimethylamino-2-propanone (5), the second one is the formation of methylglyoxal (3) via the dehydrogenation of hydroxyacetone (2), which undergoes decarbonylation to produces acetaldehyde (4), and the last one is the decomposition of hydroxyacetone (2) into formaldehyde (6) and acetaldehyde (4) (Scheme 2).41
Scheme 2 Plausible reaction pathway of the H6P2W18O62/Zr-MCM-41 catalyzed amination of glycerol with dimethylamine. |
In 2020, the group of Li demonstrated an interesting methodology for the acid–base tuned selective and switchable N-hydroxyethylation and N-acetonylation of amines employing glycerol in the presence of a Ru(II) complex.48 The stability of the active ruthenium species with glycerol coordination is essential for the selective carbon–carbon or carbon–oxygen bond cleavage of glycerol under base/acid conditions. Initially, the authors reacted N-methylaniline with glycerol applying Ru-complexes as catalysts. Various organic ligands were tested with 1 mol% RuCl2(PPh3)3 in the presence of catalytic amounts of potassium t-butoxide under an elevated temperature (Table 1, entry 10). The combination of bidentate phosphine ligand 1,1′-bis(di-cyclohexylphosphino)ferrocene (DCyPF) and thiophene-based nitrogen ligand N-MeTMA (N-methyl-(2-thienylmethyl)amine) was found to be the best ligand system for this Ru-based amination methodology to achieve 94% of the corresponding N-hydroxyethylated product (A). Under the optimized reaction conditions (0.5 mmol amine, 1.5 mmol glycerol, 1 mol% RuCl2(PPh3)3, 1.05 mol% DCyPF, 1.2 mol% N-MeTMA, 5 mol% KOtBu, 1 mL 1,4 dioxane, 150 oC, 20 h), various N-alkylanilines bearing electron-donating and withdrawing groups including halogen-substituted ones and benzo-fused cyclic motifs were reacted with glycerol and obtained the corresponding products in 41–91% yields (Scheme 3A). In addition, secondary aliphatic amines were also tested for the catalytic amination of glycerol to obtain the desired products in 43–60% yields (Scheme 3A). However, phenylamine and benzylamine did not give the targeted products.48 Besides, the authors successfully applied this Ru-based methodology for the synthesis of an anti-cancer drug molecule, showing the robustness of this protocol and possible applications of glycerol in the pharmaceutical industry (Scheme 3B).
Entry | L1 | L2 | Yield, A (%) | Yield, B (%) |
---|---|---|---|---|
a Reaction conditions: 0.5 mmol N-methylaniline, 1 mL 1,4-dioxane, 150 °C, 20 h. Conversions and yields were determined by GC using n-docecane as an internal standard. b [Ru(p-cymene)Cl2]2 was used. c No base. d 10 mol% of AcOH was used instead of tBuOK. Abbreviation: Pica = 2-picolyamine; N-MePica = 2-[(methylamino)methyl]pyridine; Hafa = 2-furfurylamine; TMA = 2-thiophenemethylamine; TEA = 2-thiopheneethylamine; N-MeTMA = N-methyl-(2-thienylmethyl)amine. | ||||
1 | — | — | n.d. | Trace |
2 | tol-BINAP | Pica | 12 | Trace |
3 | tol-BINAP | — | Trace | n.d. |
4 | — | Pica | n.d. | Trace |
5 | DCyPF | Pica | 74 | Trace |
6 | DCyPF | N-MePica | 80 | Trace |
7 | DCyPF | Hafa | 62 | Trace |
8 | DCyPF | TMA | 85 | Trace |
9 | DCyPF | TEA | 87 | Trace |
10 | DCyPF | N-MeTMA | 94 | Trace |
11b | DCyPF | N-MeTMA | 94 | Trace |
12b,c | DCyPF | N-MeTMA | Trace | 40 |
13b,d | DCyPF | N-MeTMA | n.d. | 81 |
Interestingly, by adding 20 mol% of acetic acid as a co-catalyst, the selectivity of Ru catalyst was switched to yield N-acetonylated product (B) in 81% yield (Table 1, entry 13). Based on this result, the authors extended the utilization of glycerol and reacted it with different amines under acidic conditions to afford N-acetonylation products in moderate to good yields (45–81%) (Scheme 3C).48a In the proposed reaction pathway presented in (Scheme 4), ethylene glycol (11) is produced from glycerol (1) through a retro-aldol reaction. In situ NMR experiments with labelled 13C3-glycerol and the detection of ethylene glycol (11) and hydroxyacetone (2) confirmed the involvement of a hydrogen-borrowing pathway and retro-aldol carbon–carbon bond cleavage steps (Scheme 4). The thienyl amine ligand inhibits the formation of nonlabile Ru–O interaction between the catalyst and glycerol due to the hemilabile S–Ru attachment.48a
Apart from the utilization of glycerol as an alkylating agent, biomass-derived carbohydrates also serve as excellent sources of C2 alkylating reagents of arylamines to generate β-amino alcohols in the presence of homogeneous ruthenium complexes under acidic conditions.48b
Recently, Bhanage and co-workers explored the application of various C2- and C3-feedstocks such as glycerol, 1,3-dihydroxyacetone, ethylene glycol, glycolic acid, and glyoxal for the selective synthesis of N-formamides using TBHP as oxidant.53 Both 1,3-dihydroxyacetone and glyoxal exhibited the best carbon efficiency and resulted in N-formamide in 100% selectivity.53 Subsequently, the same group reported a crystalline MnO2 nanocatalyst for the preparation of various N-formamides under aerobic conditions using glycerol.54 The selectivity of the reaction can be tuned using mixed crystalline MnO2 nanomaterials and their surface Mn(III)/Mn(IV) species ratios. In the presence of α- and γ-MnO2 the N-formamide product with high selectivity was obtained, while β- and δ-MnO2 gave the mixture of N-formamide and N-methylamine in equal ratio. Under the optimized conditions (0.5 mmol amine, 0.5 mmol glycerol, 30 mg γ-MnO2, 10 bar air:O2 (9:1), 5 mL dioxane, 90 °C, 12 h), various primary and secondary amines were selectively formylated with glycerol and provided the desired products in good to high yields (43–90%) (Scheme 6). On the other hand, o-phenylenediamine and o-amino benzonitrile failed to give the desired products. This protocol is also amenable for the gram-scale synthesis of N-formylmorpholine. Recycling and reusability of the γ-MnO2 catalyst was demonstrated for 7 times and it was found that the activity of the catalyst in each cycle was slightly dropped due to Mn leaching (Fig. 3).54
Fig. 3 Recyclability of γ-MnO2 catalyst for N-formylation. This figure has been adapted from ref. 54 with permission from Elsevier, copyright 2022. |
As shown in Fig. 4, the first step of this N-formylation reaction involves the oxidation of glycerol (1) to dihydroxyacetone (15) in the presence of morpholine (14) and MnO2 catalyst. The homolytic cleavage at the carbonyl site of the dihydroxyacetone (15) leads to the generation of radicals (16 and 17), which traps the morpholine moiety and forms activated species. By molecular oxygen the Mn(III) site is re-oxidized to Mn(IV) at a lower rate. The presence of the Mn(IV) site on the surface leads to higher selectivity of the catalyst towards N-formamide (18), whereas a mixture of Mn(III) and Mn(IV) species is responsible for the formation of a mixture of formamide and N-methylamine (1:1 ratio).
Very interestingly, Jin and Chaudhari et al.63 presented a challenging amination of glycerol (1) with ammonia to produce alkyl amines such as isopropylamine (21), ethylamine (22) and N-methylamine (23) using Ru/C (Scheme 8). To find out the best catalyst, different noble metal-based catalysts such as Ru/C, Pd/C, Rh/C and Pt/C were tested, and among these the Ru-system is found to be the optimal one. It has been observed that glycerol conversion was achieved up to 96% in 48 h of reaction in the presence of Ru/C (Table 2). With respect to the mechanism of this Ru-catalyzed amination process (Fig. 5), firstly, dehydrogenation of glycerol (1) occurs to give propane-1,2-diol (24), which then undergoes dehydration to give acrolein (8). Next, acrolein reacts with amine and generates imine (25), which on reduction provides propylamine (26). The dehydrogenation of glycerol also leads to the formation of glyceraldehyde (10) which upon cleavage gives formaldehyde (6) and glycolaldehyde (27). These intermediates proceed with three possible reaction sequences. The first possibility is to form ethylene glycol (33) and methanol (34) by simple hydrogenation. The second pathway reaction with ammonia forms imine (28), followed by hydrogenation leading to methyl amine (23). The third possibility is reaction with ammonia followed by hydrogenation to produce 2-hydroxyethylamine (31), which can be either hydrogenated or dehydrogenated to form ethylamine (22) and 2-aminoacetaldehyde (32) respectively. The 2-aminoacetaldehyde (32) can produce ethylenediamine (35) by undergoing a reaction with ammonia followed by hydrogenation.
Experimental conditions: 200 °C, 100 bar H2 pressure, 48 h. Abbreviation: methylamine (MA), ethylamine (EA), propylamine (PA), ethylene-diamine (EDA), 2,6-dimethylpiperazine (2,6-DMP), piperazine (PZ), 2-methyl piperazine (2-MP), 1,2-propanediol (1,2-PDO), methanol (MeOH), ethylene glycol (EG). | ||||
---|---|---|---|---|
# | 1 | 2 | 3 | 4 |
Catalyst | Pd/C | Rh/C | Pt/C | Ru/C |
Conversion (%) | 16.3 | 32.1 | 55.8 | 96.2 |
Selectivity (%) | ||||
MA | 3.9 | 1.5 | 11.6 | 18.6 |
EA | 0 | 0 | 3.6 | 14.4 |
PA | 0 | 3.5 | 3.0 | 15.6 |
EDA | 5.8 | 1.9 | 3.8 | 2.8 |
2,6-DMP | 51.0 | 50.1 | 29.3 | 2.9 |
PZ | 3.7 | 7.4 | 2.8 | 2.2 |
2-MP | 4.5 | 3.7 | 4.5 | 3.2 |
1,2-PDO | 1.0 | 2.8 | 0.5 | 1.5 |
MeOH | 4.8 | 1.9 | 3.8 | 15.1 |
EG | 2.1 | 1.0 | 0.6 | 2.4 |
Unknowns | 23.3 | 26.2 | 38.5 | 21.4 |
Quite recently, Bhanage and co-workers prepared N-methylamines employing β-MnO2 as a catalyst in the presence of a higher amount of glycerol.54 Under optimized conditions (0.5 mmol amine, 10 mmol glycerol, 30 mg β-MnO2, 10 bar air:O2 (9:1), 100 °C, 5 mL dioxane, 12 h), aliphatic secondary amines reacted well with glycerol and obtained the corresponding N-methylated products in average yields (24–58%) (Scheme 9). Primary amine such as aniline failed to deliver the corresponding N-methylamine product under standard conditions. Catalyst recycling experiments showed that the activity of catalysts is significantly decreased in each recycle (Fig. 6). The decrease in the catalytic activity of β-MnO2 was observed due to the Mn leaching. The catalyst β-MnO2 is active in the oxidation state of Mn(III) or Mn(IV) but the excess of glycerol concentration reduces the Mn(III) or Mn(IV) active surface into a Mn(II) surface in the last step of the reaction and leads to the higher Mn leaching content in the case of β-MnO2 which does disturb the redox cycle necessary for a good conversion and resulted in a decrease in the conversion of amines.
Fig. 6 Recyclability of β-MnO2 catalyst for N-methylation. This figure has been adapted from ref. 54 with permission from Elsevier, copyright 2022. |
For the synthesis of N-methylamine products, MnO2 was found to be a suitable oxidation catalyst. In the redox cycle of Mn(III)/Mn(IV), these reaction conditions follow a Mars–van Krevelen mechanism for the oxidation of glycerol. The first step involves the oxidation of substrate at the MnO2 surface to form partially reduced MnOx species and the second is the re-oxidation of the MnOx species in the presence of molecular oxygen. The presence of oxidative conditions is important in order to convert Mn(III) into Mn(IV), which is necessary to obtain the catalytic cycle.54
Recently, Wang and Li et al.,69 adapted the DFT M06-2X method for the synthesis of pyridine (36) by reacting glycerol (1) with ammonia at 550 °C. Based on glycerol conversion and mechanistic investigations, it was observed that the dehydration of glycerol produced acrolein (8), acetaldehyde (4), and acetone (38) as well as acetol (2). These oxygenated compounds, particularly acrolein (8) and acetaldehyde (4), react with gaseous ammonia to form imine (20, 39–41), which undergoes sequential reactions such as Michael addition, a Diels–Alder reaction, deammonization, and a dehydrogenation process to form pyridine 36 (Scheme 11).69
Like pyridine, quinoline-based scaffolds are often found in several biologically active molecules. For the synthesis of quinolines, Skraup synthesis (Scheme 12) represents one of the general methodologies in which glycerol reacts with aniline in the presence of sulphuric acid and an oxidant (nitrobenzene or As2O5).70 In 2013, Corma and Iborra together synthesized benzimidazoylquinoxaline in good yields via a one-pot oxidative coupling of glycerol or glyceraldehydes with 1,2-phenylenediamines in a two-step reaction, employing Au/CeO2 as the heterogeneous catalyst under base-free and mild reaction conditions, and air as the oxidant (Scheme 13).71 Interestingly, 1,2-phenylenediamines bearing electron-withdrawing groups improved the selectivity of the targeted benzimidazoylquinoxaline products. The Au/CeO2 catalyst could be easily recovered and re-used with a slight loss of activity, thereby maintaining high selectivity.71
In 2014, Len and colleagues performed a classical Skraup reaction in neat water under microwave irradiation conditions and synthesized 5-, 6-, 7-, and 8-substituted quinolines employing glycerol and anilines as starting materials (Scheme 14).72 This protocol is also amenable for the synthesis of phenanthrolines by treating nitroaryl derivatives with glycerol.72
After three years, the group of Chao reported the vapour-phase synthesis of quinoline (43) by reacting glycerol (1) with aniline (42) over Ni/mesoporous beta zeolite (Ni/Hβ-At) as a catalyst at 470 °C and produced quinoline in 71.4% yield (Scheme 15).73 Key to this success is the mesoporous structure and the acidic sites of the catalyst. Mesopores promote the transport of bulky products and the weak Brønsted acid sites favour the dehydration of glycerol to acrolein, as well as the existence of a Lewis acid site accelerating the formation of quinoline. The catalyst was reused only up to 3 cycles due to the deposition of coke.73 A plausible reaction mechanism was also proposed for this Ni-catalyzed synthesis of quinoline (Scheme 16). Firstly, glycerol upon dehydration produces 3-hydroxypropanal (7), acrolein (8), acetol (2), and acetaldehyde (4) which were detected by mass spectral analysis. Next, these obtained intermediates react with aniline and gave different N-heterocycles. For example, the reaction of acetaldehyde (4) and aniline (42) produced 2- or 4-methylquinoline (50 and 48 respectively). 3-Methylindole (46) was generated from the reaction of aniline (42) and acetol (2) (Scheme 16).
In 2015, Zhang and co-workers reported the synthesis of 2-methyl quinoxalines in satisfactory yields in the presence of a Ru catalyst.44 Very recently, the group of Fujita synthesized 2-methylquinoxaline derivatives by reacting 1,2-phenylenediamine with glycerol in the presence of an N-heterocyclic carbene-based Ir-catalyst.74 Various NHC-based Ir-catalysts have been screened out and it was found that the Ir-complex with an N-isopropyl group containing the NHC ligand had optimal results in the presence of K2CO3 in CF3CH2OH solvent. Under optimized conditions (1.1 mmol glycerol, 1 mmol 1,2-phenylenediamine, 1.0 mol% Ir-catalyst, 1 mmol K2CO3, and 1 mL CF3CH2OH, 20 h), different substituted 1,2-phenylenediamines were reacted with glycerol and gave a 92% yield of the corresponding 2-methylquinoxazoline (Scheme 17). Methyl-substituted 1,2-phenylenediamine gives isomers of dimethylquinoxaline in good yield. Diamine with a pyridine ring skeleton also gives the corresponding quinoxaline in moderate yield (Scheme 17).
As shown in Scheme 18, the glycerol undergoes dehydrogenation and provides an equilibrium mixture of glyceraldehyde (10) and dihydroxyacetone (15) in presence of the NHC-based Ir-catalyst. Owing to the high reactivity of glyceraldehyde, it immediately reacts with 1,2-phenylenediamine (56) and generates an intermediate (52), which undergoes dehydration to give the enol derivative (53) of 2-aminophenyliminopropan-2-one (54). Finally this derivative proceeds with intramolecular dehydration to give 2-methylquinoxazoline (55) (Scheme 18).74
In addition to the importance of bioactive molecules, oxazoline-based compounds are often used as organic ligands in asymmetric catalysis.75 Hence, the use of renewable glycerol for the preparation of oxazoline and its derived compounds is highly desired. In this regard, in 2018, Rode and co-workers reported a simple and environmentally benign approach for the catalytic synthesis of an oxazoline-based compound (57) from glycerol and ammonia.42 The authors have used two catalytic systems to produce oxazoline derivatives in different pathways. Acidic Cu–Zr catalyzed the reaction in two steps in which glycerol converts to acetol 2 (78% yield) followed by amination with ammonia to an oxazoline-based compound with 95% yield (Scheme 19). However, Ru/C catalyzed the amination of glycerol in a one-pot reaction to produce oxazoline derivative (57) with 95% selectivity (Scheme 19). In addition, the Ru/C catalyst was found to be highly active and showed an excellent performance in up to four reaction cycles.
Scheme 19 Cu and Ru-catalyzed amination of glycerol with ammonia to produce the oxazoline-based compound. |
The authors proposed a plausible mechanistic pathway for the amination of glycerol to an oxazoline derivative (Scheme 20). Initially, acid-catalysed dehydration of glycerol takes place (58–59), in which the active sites of the metal play a crucial role in the activation of glycerol (59). Next, the abstraction of primary –OH of glycerol by Ru (Ru–O) and simultaneous proton abstraction of the adjacent carbon by the bridging oxygen atom of the Ru–O leads to the formation of enol (60) which upon tautomerization is converted into keto (61) by abstraction of the proton of hydroxy group of the enol by Ru(0) to give acetol (61). The bifunctionality of the catalyst was observed because RuO2 and RuO3 act as the acid promoter for the activation of the carbonyl group whereas Ru is an active site for ammonia dissociation. NH3 dissociatively adsorbed on the catalyst surface and a simultaneous lone pair of N attacks on the acetol formed a tetrahedral intermediate (62) which is reversibly converted to carbonyl amine and then to 2-imino-1-propanol (63). The imine formation mainly requires acid sites for the elimination of water. In the last step, the formed 2-imino-1-propanol undergoes condensation (64) with a second molecule of acetol which upon cyclization leads to the formation of oxazoline derivative (57).42 Very recently, Yu and Xiao together reported a robust protocol for the synthesis of 2-methylquinoxalines directly from glycerol and o-phenylenediamine in the presence of Pt/CeO2 catalyst at 140 °C.76 The authors also tested other bio polyols to produce high-value 2-methylquinoxalines.
Scheme 20 Plausible mechanistic pathway for the amination of glycerol to the oxazoline-based compound using heterogeneous Ru-catalyst. |
Fig. 7 Catalytic conversion of glycerol into alanine in a batch reactor over (a) Ru1M10/MgO, Ru/MgO, Ni/MgO and RANEY® Ni catalysts, (b) Ru1Ni10 on different supports (W indicates catalysts prepared by the wet-impregnation method), (c) MgO supported Ru1NiX catalyst with varied Ru:Ni ratio, and (d) conversion/yield profile over Ru1Ni7/MgO catalyst as a function of time. Reaction conditions: 100 mg glycerol, 200 mg NaOH, 67 mg catalysts or 30 mg RANEY® Ni (Ru:substrate molar ratio = 0.012), 2 mL NH3H2O (25 wt%), 10 bar H2, 220 °C, 4 h. Catalysts were reduced at 500 °C for (a–c) and 600 °C for (d). This figure has been adapted from ref. 45 with permission from Wiley, copyright 2019. |
The authors have made an interesting experiment by recording the 13C NMR spectrum of the product mixture using glycerol–13C3 as the starting material. The 13C NMR of the product mixture was simple throughout the complete reaction time of either 1 or 4 hours (Fig. 8). During the course of this amination of glycerol, lactic acid and alanine were identified as the major products. In addition, small amounts of 13C formic acid, formamide and 13C2 glyceric acid were also observed. Based on these results, the authors proposed a plausible reaction pathway, which is presented in (Fig. 9). First, lactic acid (66) is produced from glycerol (1) via sequential dehydrogenation, dehydration, and rearrangement reactions. Then the –OH group of the lactic acid (66) reacts with NH3 to form alanine (69) by a borrowing-hydrogen methodology. The other C1 and C2 side products were formed by the hydrogenolysis of glycerol. In this amination process, the catalyst and base cooperatively work by a tandem reaction sequence involving dehydrogenation, hydrogenation, and hydrogenolysis as well as dehydration and a Cannizzaro reaction. The base also facilitates the metal-catalyzed dehydrogenation of glycerol by deprotonation and most likely displaces lactic acid/alanine from the catalyst surface as sodium lactate/sodium alaninate, which accounts for the proportional rise in lactic acid and alanine yields with respect to the amount of NaOH (Fig. 9).
Fig. 8 13C NMR spectra of alanine and lactic acid produced by the Ru1Ni10/MgO catalyzed amination of glycerol with ammonia. This figure has been adapted from ref. 45 with permission from Wiley, copyright 2019. |
Fig. 9 Proposed reaction mechanism for the synthesis of alanine from glycerol and ammonia in the presence of Ru1Ni10/MgO. |
Fig. 10 Catalyst re-usability and regeneration for Pd supported on simple oxide materials. This figure has been adapted from ref. 79 with permission from the Royal Society of Chemistry 2020. |
In 2018, the group of Milstein reported a manganese pincer complex for the synthesis of 2-methyl quinoxaline (55) in 80% isolated yield by the dehydrogenative coupling of propane-1,2-diol (75) and ortho phenylenediamine 56 (Scheme 22).83
In 2019, Kundu and co-workers reported a novel and robust method for the synthesis of 2-methyl quinoxaline (55) in an aqueous environment employing propane-1,2-diol (75) and benzene-1,2-diamine (56) under atmospheric conditions.84 Subsequently, the same group also reported a N-doped carbon-supported cobalt catalyst for the synthesis of 2-methyl quinoxaline (55) in 93% yield.85 Interestingly, the combination of NiBr2/1,10-phenanthroline also worked well for the preparation of 2-methyl quinoxaline (55) in excellent yield.86
In 2019, Yue and co-workers reported the selective catalytic amination of 1,2-propanediol (75) with NH3 over nano-Co/La3O4 and achieved a 68% conversion and 89% selectivity of 2-amino-1-propanol (76) under optimal conditions (Scheme 23).87 The authors also revealed that the presence of basic lanthanum oxide was essential to facilitate the selective catalytic reaction.
Despite its notable advantages, there are still challenges in the reaction of glycerol that need to be addressed. One most important challenge is its efficient and highly selective conversion to produce the desired compounds in high yields. Due to the difficulty in the reactivity of glycerol, its application in organic synthesis is less explored. To accomplish these challenges, the development of potential and sustainable catalytic methodologies is the key factor. In particular, the design of highly active and selective catalysts that should convert glycerol in mild conditions is of prime importance. Next, to understand and to solve the complexity of the reaction of glycerol, tools for mechanistic and kinetic investigations need to be strengthened. Glycerol is an ‘ideal’ feedstock and its utilization capacity needs to be increased to produce both fine and bulk chemicals as well as for the preparation of pharmaceuticals and agrochemicals.
Presently, the majority of industrially important amines are produced from fossil-based feedstocks. Owing to the excess availability of glycerol in a form that is comparatively low cost, its conversion into the possible organonitrogen chemicals will not only mitigate the carbon footprint but also bring incentives to the chemical industries and have the potential to become a renewable alternative to fossil fuels. Recent achievements in the catalytic amination of glycerol and its derived molecules to produce amine-based functional compounds will likely support the further advancements of this research area. Therefore, a collaboration between academia and industry is critical to achieve this goal.
We sincerely hope that this review will be useful to the scientific community working in the area of valorization of glycerol and biomass-based feedstocks as well as organic synthesis, amines, heterocycles, and catalysis.
Footnote |
† Authors have equally contributed. |
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