Maria Arkhipova,
Svetlana Eichel and
Gerhard Maas*
Institute of Organic Chemistry I, University of Ulm, Albert-Einstein-Allee 11, 89081 Ulm, Germany. E-mail: gerhard.maas@uni-ulm.de; Fax: +49-731-5022803
First published on 27th October 2014
The solubility of titanium and aluminium alcoholates and of titanium tetrakis(trimethylsilanolate) in several hexaalkylguanidinium-based room temperature ionic liquids was screened. The solvent/solute combinations which displayed the highest alcoholate solubility and stability were applied as Lewis-acidic catalytic media for several dehydrating cyclocondensations: lactamisation of ω-aminocarboxylic acids, direct amidation of carboxylic acids, synthesis of oxazolines from carboxylic acids and 2-aminoethanol, lactonisation of 6-hydroxyhexanoic acid, and Paal–Knorr synthesis of pyrroles.
The ionic liquids used as reaction media are usually based on 1,3-dialkylimidazolium, N-alkylpyridinium, tetraalkylammonium, N,N-dialkylpyrrolidinium, and tetraalkylphosphonium cations. Strangely enough, hexaalkylguanidinium-based ILs are often ignored in review articles and book chapters. As alternative reaction media, all aspects named above also apply to hexaalkylguanidinium-based ILs, and indeed some applications as reaction media in organic synthesis and catalysis have been reported. Guanidinium-based phosphotungstates were used for epoxidation of olefins,13 guanidinium acetates as media for the palladium-catalysed Heck reaction,14 and Lewis acidic guanidinium ILs for aminolysis of epoxides.15 Hexaalkylguanidinium ILs as reaction media have been reported for the oxidation of benzyl alcohols,16 nucleophilic substitution reactions,17 CO2 fixation,18 Sharpless dihydroxylation19,20 and asymmetric aldol reaction.21,22 Intramolecular carbenoid C–H insertion of an α-methoxycarbonyl-α-diazoacetamide was successfully performed with rhodium or ruthenium catalysts in hexaalkylguanidinium triflates.23
Hexaalkylguanidinium salts show high chemical stability, due to the superior charge delocalisation in the cation, and are thermally remarkably stable.24,25 Another advantage of guanidinium ionic liquids consists in the possibility to vary up to six substituents to adjust the properties of the IL to a specific task.24–27 In this paper we describe a new application of guanidinium-based ionic liquids as reaction media containing a titanium or aluminium alcoholate as a mild Lewis-acidic catalyst for several (cyclo)condensation reactions.
Titanium alkoxides (Ti(OR)4 and MeTi(OR)3) have been widely applied as Lewis acids, for example in aldol reactions,28,29 in Kulinkovich cyclopropanation,30 and in the formation of lactams. Titanium tetraisopropoxide is also a reagent for the Sharpless asymmetric epoxidation of allylic alcohols.31
Compound | R1 = R2 | R3 = R4 | R5 = R6 | X | |
---|---|---|---|---|---|
1a | [N11N22N44Gu]OTf | Me | Et | Bu | OSO2CF3 |
1b | [N11N22N1O21O2Gu]OTf | Me | Et | MeO(CH2)2 | OSO2CF3 |
2a | [N11N22N44Gu]NTf2 | Me | Et | Bu | N(SO2CF3)2 |
2b | [N22N44N66Gu]NTf2 | Et | Bu | Hex | N(SO2CF3)2 |
2c | [N11N22N1O21O2Gu]NTf2 | Me | Et | MeO(CH2)2 | N(SO2CF3)2 |
2d | [N11N11N1O21O2Gu]NTf2 | Me | Me | MeO(CH2)2 | N(SO2CF3)2 |
2e | [N11N11N66Gu]NTf2 | Me | Me | Hex | N(SO2CF3)2 |
2f | [N11N66N66Gu]NTf2 | Me | Hex | Hex | N(SO2CF3)2 |
3a | [N22N44N66Gu]N(CN)2 | Et | Bu | Hex | N(CN)2 |
Solubility tests (Table 2) showed that aluminium isopropoxide is not soluble in hexaalkylguanidinium ILs at room temperature and can be dissolved only at 120–130 °C, whereas titanium isopropoxide dissolves readily in liquid guanidinium bis(triflamides) with longer alkyl chains in the cation at room temperature. Interestingly, the metal alcoholates are only sparingly soluble in the ether-functionalised guanidinium salts, although it was expected that Lewis acid/Lewis base interactions would favour the dissolution. For comparison we also checked some commonly used salts, such as 1-butyl-3-methylimidazolium and hexyl-trimethylammonium bis(triflamides). It was noted that several of the guanidinium-based ILs are better solvents for titanium isopropoxide than the examined imidazolium and ammonium salts.
IL | Ti(OiPr)4 | Al(OsecBu)3 | Al(OiPr)3 | |
---|---|---|---|---|
a Mass-to-volume ratio in those cases, where suspensions or two phases were formed. | ||||
1a | [N11N22N44Gu]OTf | 0.17 (turbid) | 0.01 (turbid) | |
1b | [N11N22N1O21O2Gu]OTf | 0.05 (turbid) | 0.12 (turbid) | 0.16 (turbid) |
2a | [N11N22N44Gu]NTf2 | 0.11 (clear) | 0.06 (turbid) | |
0.40 (turbid) | ||||
2b | [N22N44N66Gu]NTf2 | 0.84 (clear) | 0.37 (turbid) | 0.44 (turbid) |
3.00 (turbid) | ||||
2c | [N11N22N1O21O2Gu]NTf2 | 0.31 (turbid) | 0.01 (turbid) | |
2d | [N11N11N2O12O1Gu]NTf2 | 0.17 (turbid) | 0.24 (turbid) | 0.13 (turbid) |
2e | [N11N11N66Gu]NTf2 | 0.67 (clear) | ||
1.00 (turbid) | ||||
2f | [N11N66N66Gu]NTf2 | 0.53 (clear) | 0.14 (turbid) | 0.15 (turbid) |
3a | [N22N44N66Gu]N(CN)2 | 0.44 (clear) | 0.32 (turbid) | |
[BMIm]NTf2 | 0.20 (turbid) | 0.06 (turbid) | ||
[Me3HexN]NTf2 | 0.39 (turbid) | 0.04 (turbid) |
Solutions of titanium and aluminium isopropoxides in N,N-dibutyl-N′,N′-diethyl-N′′,N′′-dihexylguanidinium bis(trifluoromethylsulfonyl)imide (2b) or more easily obtainable N,N-dihexyl-N′,N′,N′′,N′′-tetramethylguanidinium bis(trifluoromethylsulfonyl)imide (2e), as the most concentrated and stable ones, were chosen for further investigations and applied as mild catalytic media for some typical dehydrating condensation reactions. Our attention was attracted mostly by bis(triflamide)-ILs, which are among the most hydrophobic ILs. This could have a positive impact on the stability and therefore activity of the catalyst and could facilitate the recovery and reuse of the IL.
We have studied the cyclisation of some ω-amino acids in guanidinium-based ILs with the goal to find a replacement for the less desirable solvent dichloroethane34 that was used in the reported procedure. Additionally we expected that the reaction could be run at higher temperature in the IL and the amount of the Ti-alkoxide catalyst could so be reduced considerably. We found that a complete conversion could be achieved within 3–5 h at 120 °C with only 5–10 mol% of catalyst.
Initial screening and optimisation reactions were carried out with 4-aminobutyric acid in a clear solution of Ti(OiPr)4 in [N22N44N66Gu]NTf2 (2b) (Table 3). The nature of guanidinium-based IL does not influence significantly the reaction time ([N22N44N66Gu]NTf2 (2b), [N11N22N44Gu]NTf2 (2a), [N11N11N66Gu]NTf2 (2e) and [N22N44N66Gu]N(CN)2 (3a) were also tested as solvents and showed similar results), and isolation of the product by bulb-to-bulb distillation was more effective than an extractive work-up procedure.
Ti(OiPr)4, mol% | Temperature, °C | |||
---|---|---|---|---|
40 | 80 | 100 | 120 | |
0 | — | |||
5 | 5 h | |||
10 | >10 h | 3 h | ||
20 | 4 h | 2 h | ||
50 | >8 h | 3 h | 2 h |
The results obtained for the cyclisation of various ω-amino acids (4-aminobutyric acid, 4-(methylamino)butyric acid, 5-aminovaleric acid, 6-aminocaproic acid) under optimised IL conditions (10 mol% of catalyst, 120 °C, distillative work-up) and under “traditional” conditions (halogenated organic solvent) are compared in Table 4. For comparison, the experiments using Ti(OiPr)4 as a catalyst were also carried out with the same quantity of catalyst in an organic solvent (1,2-dichloroethane).
Entry | n, R | Ti(OiPr)4 (50 mol%), DCEc, 84 °C | Ti(OiPr)4 (10 mol%), DCE, 84 °C | Ti(OiPr)4 (10 mol%), IL, 120 °C | Ti(OSiMe3)4 (10 mol%), IL, 120 °C | Al(OiPr)3 (10 mol%), IL, 120 °C |
---|---|---|---|---|---|---|
a DCE = 1,2-dichloroethane; IL: [N11N11N66]NTf2 (2e) or [N22N44N66]NTf2 (2b).b ILs 2e and 2b gave similar yields under the same conditions.c Ref. 32.d For comparison: a yield of 86% was achieved when the reaction was run in IL 2e at 84 °C for 3 h. | ||||||
1 | 2, H | 93% (3 h)d | 85% (3 h) | 85% (3 h) | 88% (3 h) | 89% (3 h) |
2 | 2, Me | 85% (5 h) | 41% (5 h) | 82% (3 h) | 88% (1 h) | 84% (1 h) |
3 | 3, H | 75% (4 h) | 87% (4 h) | 82% (2 h) | 94% (2 h) | 94% (3 h) |
4 | 4, H | 35% (26 h) | 9% (26 h) | 58% (26 h) | 62% (26 h) | 26% (26 h) |
In most cases the lactam yield was increased along with the expected reduction in reaction time. The system metal alcoholate/guanidinium IL was especially effective for the synthesis of the N-substituted lactam (the reaction duration was up to five times lower, entry 2) and for ε-caprolactam (during the same time the yield was almost doubled, entry 4).
Beside titanium isopropoxide other, somewhat less moisture sensitive, Lewis acids were tested. Titanium trimethylsilanolate turned out to be a bit more catalytically active in comparison to isopropanolate. Titanium 2-ethylhexanolate, which is more viscous than the isopropanolate and trimethylsilanolate, is somewhat less active than the others. This is why the reactions with titanium 2-ethylhexanolate were not extended. Aluminium isopropanolate did not show good solubility, but its catalytic activity proved to be quite similar to titanium trimethylsilanolate with one exception (synthesis of caprolactam). In order to accelerate the reaction we added molecular sieves 4 Å to adsorb the water produced in the condensation reaction and to prevent the hydrolysis of the catalyst. Notably, this had no impact on the reaction – for the reasons that became clear later (vide infra).
Another major advantage of our IL strategy is given by the fact that the IL/catalyst system could be reused in subsequent cycles with little or no reduction in yield (Table 5). To this end, the produced lactam was separated from the reaction mixture by vacuum distillation, and the IL/catalyst system, which contained a white precipitate, was used again for the next reaction cycle.
n, R | Catalyst | Yields in four cycles, % |
---|---|---|
a For reaction conditions, see Table 4. | ||
2, H | Ti(OiPr)4 | 85 – 85 – 94 – 85 |
2, H | Ti(OSiMe3)4 | 88 – 91 – 89 – 85 |
2, H | Ti(O-2-ethylhexyl)4 | 75 – 75 – 54 – 50 |
2, H | Al(OiPr)3 | 89 – 89 – 89 – 95 |
2, Me | Ti(OiPr)4 | 82 – 92 – 94 – 77 |
2, Me | Ti(OSiMe3)4 | 88 – 90 – 87 – 94 |
3, H | Ti(OiPr)4 | 82 – 79 – 74 – 72 |
3, H | Ti(OSiMe3)4 | 94 – 98 – 96 – 96 |
3, H | Al(OiPr)3 | 94 – 96 – 95 – 95 |
Moreover, the possibility of phase separation into a product phase and catalyst/IL phase was investigated, as this would facilitate the work-up procedure. To this end, the concentration of the amino acid in the usual amount of IL was increased. Unfortunately, the formed lactam did not appear as a separate phase, and a distillative work-up was required. A three times higher concentration of 4-aminobutanoic acid in the ionic liquid increased the yield of butyrolactam from 85 to 96%.
To test the scope of the developed method, the cyclodehydration of 11-aminoundecanoic acid was tried. The experiment failed, perhaps mainly due to the low solubility of the amino acid in the IL. Cyclisation of the optically active L-lysine was also attempted, but the reaction with 10 mol% of Ti(OiPr)4 at 120 °C took almost two days and yielded less than 18% of α-amino-ε-caprolactam, not in pure form. The reaction with 100 mol% of the same catalyst gave 27% of impure product, so the racemisation of the product could not be checked.
Obviously, the lactamisation is catalysed by metal alcoholates or species derived therefrom. Without catalyst no reaction takes place, also not after 5 h at 120 °C (Table 3). NMR spectra of the reaction mixture before the second cycle no longer contained signals of the isopropyl substituent. The reason could be the hydrolysis of Ti(OiPr)4 with possible formation of TiO2. Nevertheless, the solid species formed (a precipitate appeared several minutes after the start of the reaction) is catalytically active in the subsequent cycles.
Some experiments were performed to understand the nature of the catalyst. To this end, several mixtures containing a white precipitate, which remained after the product isolation by bulb-to-bulb distillation or extraction, were diluted in dichloromethane, filtered, and the precipitate was dried. NMR and IR spectra indicated the presence of 4-aminobutanoic acid in admixture with TiO2. This powder was washed with water to remove the acid. X-ray diffraction (XRD) measurements of the solid so obtained showed that it was only amorphous material. After calcination at 550 °C for 4 h, the XRD spectrum of pure anatase was obtained (Fig. 1).
Actually, it was not surprising to obtain anatase particles as a by-product of the reaction. It is well known that diverse ionic liquids are effective for the synthesis of TiO2 anatase nanoparticles from titanium alcoholates.35–38 Therefore, it was also interesting to get information on the size of particles obtained after the first reaction cycle. The TEM images of the anatase (obtained after calcination) are presented in Fig. 2 (left). Most particles are nanoparticles with a size of 30–60 nm. The image on the right shows the particles obtained after filtration from the catalyst/IL system. It is seen that they are bigger in size, the majority of them is conglomerated, and the single particles have a very porous structure.
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Fig. 2 TEM images of anatase particles (left, length scale corresponds to 30 nm) and catalyst particles (right, length scale corresponds to 60 nm). |
Is the titanium dioxide the active catalytic species? To answer this question the experiment (lactamisation of 4-aminobutanoic acid in IL 2e) with 10 mol% of anatase as a catalyst was carried out, but no reaction was observed. Notably, after addition of some drops of water the reaction set in but proceeded very slowly. On the other hand, when the powder obtained from the reaction mixture by filtration (when Ti(OiPr)4 was used as catalyst) was applied one more time, the reaction was fast as usual. With the precipitate (TiO2) washed with water only a slow reaction was observed. There was no reaction in the IL sample remaining after filtration. So the possible catalyst could be (a) the freshly precipitated Ti(OH)4, its dimers or trimers39–41 or freshly obtained TiO2 (further written as TiO2*), (b) the mentioned Ti species complexed with amino acid. For clarification, the lactamisation of 4-aminobutanoic acid was carried out in the presence of a TiO2*/amino acid complex, which had been prepared separately from Ti(OiPr)4 and 4-aminobutanoic acid in isopropanol at reflux for 3 h with subsequent filtration of the catalyst. Under analogous reaction conditions (IL 2e, 10 mol% of catalyst, 120 °C, 3 h), a conversion of 58% was determined by 1H NMR spectroscopy with the TiO2*/amino acid catalyst, compared to 99% with Ti(OiPr)4 as catalyst. Further experiments with freshly precipitated TiO2* (from Ti(OiPr)4/H2O in isopropanol) and in situ precipitated TiO2* in IL (from Ti(OiPr)4/H2O in IL 2e) showed the same catalytic activity as in the original reaction.
Concluding the obtained results, it seems that in the first reaction cycle, the reaction starts with Lewis acidic Ti(OiPr)4 as the catalyst. Ti(OiPr)4, which is sensitive even to traces of water, is hydrolysed by water formed as a side product to yield Ti(OH)4 and finally titanium dioxide. It is also known that titanium alcoholates and titanium hydroxide are prone to form oligomers.39–41 So a number of species could act as a catalyst, but the most likely under our conditions (elevated temperature, vacuum distillation) is titanium dioxide in the form of nanoparticles with porous structure (Fig. 2, right). Water is known to adsorb both associatively and dissociatively (as HO−) on the surface of titania containing reduced Ti cations and to oxidise the surface,42,43 thus blocking the coordinatively unsaturated sites at the TiO2 surface. The amino acid could be adsorbed on the surface of titanium dioxide, where the reaction takes place. Moreover, TiO2 reveals Lewis acidic properties, as well as Lewis basic properties.44 In any case, the chemical behaviour of both Ti4+ (Lewis acid) and O2− (Lewis base) ions depends on the surface structure.45 It seems that in this reaction we deal with mildly Lewis acidic titanium dioxide as catalytic species. Moreover, Lewis acid activity of TiO2 nanoparticles has already been reported.46,47
With the application of hexaalkylguanidinium bis(triflamides) as solvents we managed: (a) to lower the amount of the catalyst significantly, (b) to reduce the reaction time (since the IL allows a higher reaction temperature), (c) to use an easier work-up procedure (vacuum distillation of the product from the reaction mixture), (d) to carry out several cycles without regeneration of IL and without extra addition of new catalyst before the next cycle, (e) to improve yields in some cases and (f) to avoid the use of organic solvents and some disadvantages associated with them (e.g. volatility, flammability, disposal of chlorinated solvents etc.).
For the optimisation purposes the reaction between phenylacetic acid and piperidine furnishing benzamide 4 (Scheme 2) was chosen. The same approach as for the lactamisation reaction was taken: the catalyst quantity and temperature were varied (Table 6), and the product was separated through bulb-to-bulb distillation. These experiments showed the suitability of this system for the investigated reaction, as very good yields could be achieved and only 10–20 mol% of the catalyst was required. For reactions with other substrates the conditions with 20 mol% of Ti(OiPr)4 and at 90 °C were selected. For the synthesis of phenylacetyl piperide, replacement of IL 2e with 1-butyl-3-methylimidazolium bis(triflamide) [BMIM]NTf2 as the solvent did not significantly affect reaction time and yield at several temperatures and catalyst loadings. The results of the direct amidation reactions of phenylacetic acid or benzoic acid with secondary and primary amines are presented in Table 7. For comparison, amide formation from phenylacetic acid and piperidine (at 100 °C), morpholine (at 100 °C) or benzylamine (at 70 °C) in dry THF, in the presence of Ti(OiPr)4 (20–10 mol%) and 4 Å molecular sieves, succeeded in yields of 69, 76 and 91% after chromatographic purification.49
Catalyst, mol% | Temperature, °C | |||
---|---|---|---|---|
77 | 90 | 120 | 200 | |
0 | 74% (6 h) | |||
10 | 90% (9 h) | 90% (7 h) | 90% (5 h) | 91% (4 h) |
20 | 91% (7 h) | 94% (4 h) | 93% (3 h) | 92% (2 h) |
50 | 91% (7 h) | 92% (4 h) | 93% (2.5 h) | 94% (2 h) |
Acid | Amine | ||
---|---|---|---|
Piperidine | Morpholine | Benzylamine | |
Phenylacetic acid | 94% (4 h) | 92% (4 h) | 92% (4 h) |
Benzoic acid | 94% (5 h) | 92% (6 h) | 92% (7 h) |
As in the case of lactamisation it was desirable to develop a recyclable system for direct amidation in a guanidinium-based IL. The first experiments showed that the second cycle of the reaction required a longer time. To reduce this time, 3 Å molecular sieves were added in the second cycle. Reactions were also performed at higher temperatures than in the first cycle (Table 8). Under the optimal conditions (20 mol% of catalyst at 200 °C), four subsequent cycles could be performed in a short time with good yields (92% – 91% – 91% – 87%).
Although the recyclability of the direct amidation reaction of phenylacetic acid and piperidine in IL has been achieved, the procedure for reuse of the catalyst/IL system was not developed further for other substrates because of the high temperatures needed in the first case. To improve the reaction conditions, more effective Lewis acids may be required.51
Methods of synthesis of 2-oxazolines have been explored extensively. Some of the cyclocondensations of carboxylic acids with 2-aminoalcohols suffer from using such harsh reagents as thionyl chloride and the necessity of high temperature conditions (up to 230 °C).57,58 Several milder approaches have also been developed, including preferable one-pot procedures. One of the most facile one-pot protocols utilises a tetranuclear zinc cluster in refluxing toluene,59 providing a number of oxazolines in good and excellent yields after chromatographic work-up. Another approach consists in the use of a [BMIm]Cl/InCl3 system, which affords 60–80% yields under mild conditions (60 °C, 3 h).60 Nevertheless, in order to obtain the pure products organic solvents were needed, and nothing was reported about the possibility of recycling the catalyst/IL system.
In order to develop an efficient procedure with a recyclable catalyst system, we explored Ti(OiPr)4/[N11N11N66Gu]NTf2 (2e) as a milieu for the direct dehydrating condensation. By analogy to the lactamisation and direct amidation reactions reported above, this system was expected to catalyse at least the first step in the oxazoline synthesis, namely amide formation (Scheme 3). The application of a thermally more stable guanidinium bis(triflamide) IL (instead of imidazolium chloride) would allow to work at higher temperatures.
For the initial studies the reactions of benzoic acid with either monoethanolamine (MEA) or 2-amino-2-methyl-1-propanol were taken. In refluxing chlorobenzene the reactions needed 67 h and 120 h, respectively, to afford after chromatographic work-up the oxazolines in yields of only 40 and 50% (Table 9). The first experiments (benzoic acid with MEA) in IL showed that at 120 °C solely N-(2-hydroxyethyl)-benzamide is formed. However, the oxazolines could be obtained after bulb-to-bulb distillation at 200 °C instead of 120 °C during several hours. This means that the cyclic product was formed during distillation. When the whole reaction was conducted at 200 °C, formation of the oxazoline was observed in the NMR spectra, but the product could be isolated only in poor yields. To lower the required reaction time, the reaction mixture was kept at first at 120 °C for the amide formation, and then the temperature was increased to 200 °C. Unfortunately, all attempts led only to poor yields. A higher amount of catalyst (Ti(OiPr)4) accelerated the reaction, but high temperatures were still needed for the oxazoline formation. As a disadvantage, titanium tetraisopropoxide was distilled off together with the product; this means that the catalyst was not immobilised in the IL and therefore could not be used once more. In addition, the product had to be separated from the catalyst, and so the extraction with an organic solvent was unavoidable.
Solvent | Cat.b, mol% | Conditions | Yield, % | Solvent | Cat.b, mol% | Conditions | Yield, % |
---|---|---|---|---|---|---|---|
a IL = [N11N11N66Gu]NTf2 (2e).b Catalyst = Ti(OiPr)4.c Not obtained in pure form; chromatographic purification or distillation was necessary. | |||||||
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PhCl | 50 | 140 °C/67 h | 40 | PhCl | 50 | 140 °C/120 h | 51 |
ILa | 50 | 200 °C/20 h | 23c | IL | — | 200 °C/7 h | 18 |
IL, MS 4 Å | — | 120 °C/1 h + 200 °C/15 h | 0 | IL, MS 4 Å | — | 200 °C/7 h | 49 |
IL | 250 | 120 °C/2 h + 200 °C/7 h | 52 | IL, MS 4 Å | 50 | 120 °C/1 h + 200 °C/8.5 h | 67 |
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IL, MS 4 Å | 50 | 200 °C/6 h | 11 | IL, MS 4 Å | 50 | 120 °C/1 h + 200 °C/7 h | 63 |
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IL, MS 4 Å | 50 | 120 °C/4 h + 200 °C/7 h | 34 |
This reaction suffers from poor yields and the necessity of high temperatures, likely because the Lewis acid used is not strong enough to activate the carboxylic acid. To improve the reaction conditions, an attempt with MW irradiation was made, but also after several hours only the benzamide was produced. Aluminium isopropoxide and titanium tetrakis(trimethylsilanolate) were found to be even less effective than titanium tetraisopropoxide.
As the reaction required a temperature of 200 °C in all cases, the question arose, whether it was catalysed or was simply promoted by the temperature and/or molecular sieves. In the case with monoethanolamine no reaction took place without the catalyst; in the case of 2-amino-2-methyl-propanol, unexpectedly, a 49% yield was obtained with molecular sieves and 18% without molecular sieves and catalyst. It can be concluded that the catalyst plays only a limited role in this reaction and that the nucleophilicity of the amine is a key factor for the reaction under these conditions.
Nevertheless, with the Ti(OiPr)4/IL system we were able to obtain 34% of bis-oxazoline 9 from dimethyl malonate after fractionating distillation (Table 9); this is still acceptable when considering the traditional multi-step synthesis of bis(oxazolines) involving corrosive acid chlorides or hazardous halogenating reagents.
For the synthesis of oxazolines 6 and 8, which gave the highest yields under optimised reaction conditions, we have also checked the reusability of the catalyst/IL system left after distillative separation of the product. In both cases, the yields of 6 and 8 decreased only slightly over three cycles and furthermore, we observed that the reaction was complete in a shorter time (Table 10).
To summarise, satisfactory conditions and yields of the 2-oxazoline synthesis were not achieved. Too high temperatures, low yields of oxazolines in many cases and the presence of the corresponding carboxamide as a side-product do not promote this procedure for a wide application, taking into account that some methods of oxazoline synthesis with high atom economy already exist. However, the low price of titanium tetraisopropoxide can in some cases be more favourable in comparison to more effective but also more expensive catalysts.
Two reasons for the failure of lactonisation could be mentioned. Firstly, the competitive dimer formation, which was also observed in controlling NMR spectra. Along with signals of the ε-caprolactone in a 1H NMR spectrum taken in D2O at δ = 4.32 (m, CH2O) and 2.67 ppm (m, CH2C(O)), signals with smaller chemical shifts appear at δ = 4.08 (m, CH2O) 2.38 ppm (m, CH2C(O)), which were tentatively assigned to the dimer 11 shown in Scheme 4 (other signals of the product and by-product were overlapped by the signals of IL). This side reaction could perhaps be suppressed by carrying out the reaction with a low concentration of hydroxy acid, but in the case of ionic liquids this is not reasonable because of the high cost of the solvent. Another reason could be the relatively low Lewis acidity of the Ti(OiPr)4 in combination with the lower nucleophilicity of the oxygen of the hydroxy acid compared to nitrogen of the amino acid used for lactamisation.
Up to day a great number of pyrrole syntheses exists, of which the Paal–Knorr condensation is the most simple, straightforward reaction, which consists in an acid-catalysed cyclisation of a 1,4-dicarbonyl compound and ammonia or a primary amine. Although this reaction was first reported concurrently by C. Paal62 and L. Knorr63 already in 1884, it still awakes the interest of researchers, who continue to develop new catalysts and solvents to render the reaction “green”. Noteworthy, a Paal–Knorr condensation is one of the steps in the synthesis of atorvastatin, a drug for lowering cholesterol levels.64,65
Both Brønsted and Lewis acids catalyse the Paal–Knorr reaction. The moderate Lewis acid Ti(OiPr)4 was employed in the synthesis of the alkaloid funebrine.66,67 It offered itself as a suitable catalyst, which would not catalyse polymerisation of pyrrole and decomposition of the aminolactone (which is a part of the funebrine structure), as in the case of stronger Lewis acids.67,68 Several papers have already reported the use of imidazolium-based ionic liquids as reaction media in the Paal–Knorr pyrrole synthesis; [BMIM]BF4 was used alone69 or in combination with catalytic bismuth(III) triflate,70 and [BMIM]HSO4 served as both a solvent and a Brønsted acid.71 We tried our reusable IL/catalyst system in this reaction type.
The condensation of 2,5-hexanedione and benzylamine to give pyrrole 12 (R1 = Bn) was investigated first (Scheme 5, Table 11). In the IL [N11N11N66Gu]NTf2 (2e), this reaction went to completion without catalyst at room temperature within 24 h; this is nearly twice as efficient than in the traditional solvent (benzene, Table 11), but distinctly slower than the reported reaction in the ionic liquids [BMIM]BF4 and [BMIM]I.69 The reaction could be accelerated not only at higher temperature, but also at ambient temperature by addition of 10 mol% of Ti(OiPr)4. Bulb-to-bulb distillation provided pure product without tedious work-up.
Further reactions were carried out with other, less nucleophilic (aniline) and more nucleophilic but sterically more hindered amines (tBuNH2, cHexNH2), in order to reveal the scope of the IL/catalyst system (Table 12). If the reaction was not complete after 24 h at room temperature, the catalyst amount was increased to 50 mol%. In some cases higher temperatures were needed. The reaction conditions were optimised for each case to improve the yields. Notably, the Paal–Knorr reaction failed completely, when tert-butylamine was used as an amine component. It is known that the Paal–Knorr reaction is a convenient synthesis of pyrroles from ammonia or primary amines, whereas sterically hindered tert-alkylamines are not prone to form pyrroles under mild conditions.72 The Paal–Knorr pyrrole synthesis was also successfully extended to the synthesis of 1-phenylpyrazole (13) from 2,4-pentanedione and phenylhydrazine (Scheme 5). In all cases, the catalyst/IL mixture remaining after product distillation could be reused several times with product yields remaining more or less unaltered (Table 13).
Diketone | Amine | Cat.a, mol% | Temp., °C | Time, h | Yield, % |
---|---|---|---|---|---|
a Catalyst = Ti(OiPr)4.b Conversion of 1,4-diketone (determined by 1H NMR). | |||||
CH3CO(CH2)2COCH3 | BnNH2 | 10 | 20 | 2 | 93 |
PhNH2 | 10 | 20 | 22 | 56b | |
PhNH2 | 50 | 20 | 48 | 94 | |
cHexNH2 | 10 | 20 | 22 | 32b | |
cHexNH2 | 50 | 20 | 20 | 45b | |
cHexNH2 | 10 | 120 | 3 | 73 | |
t-BuNH2 | 10 | 20 | 24 | 0 | |
t-BuNH2 | 100 | 20 | 24 | 0 | |
CH3COCH2COCH3 | PhNHNH2 | 10 | 20 | 24 | 95 |
The catalytic system of Ti(OiPr)4 in the hexa-alkylguanidinium bis(triflamide) 2e proved to be an effective and mild milieu for the Paal–Knorr reaction with all the advantages, which were also achieved when performing lactamisation reactions in guanidinium ILs. Pyrroles and pyrazoles can be obtained by the developed method easily and in high yields. In comparison to the procedure described by B. Wang et al.,69 who demonstrated the preparation of pyrroles in [BMIm]I at room temperature with an ensuing extraction of the product with diethylether, our procedure avoids the use of volatile and flammable organic solvents. On the other hand, the [BMIm]I system allows the synthesis of pyrroles from more sterically hindered amines, such as tert-butylamine and isopropylamine. Compared with the Bi(OTf)3/[BMIm]BF4 system proposed by Y. S. Yadav et al.,70 the developed guanidinium-based IL/Ti(OiPr)4 system has two advantages: the catalyst used is considerably cheaper and a bis(triflamide)-based IL is water-stable in contrast to an IL tetrafluoroborate.
The same catalyst/IL system is also suited to perform the direct amidation of carboxylic acids with benzylamine and cyclic secondary amines at moderately high temperatures (typically 90 °C), but its reuse in subsequent reaction cycles requires a much higher temperature (200 °C) to proceed in a short time and in high yield. A direct amidation is also included in the synthesis of 2-oxazolines from carboxylic acids and 1,2-aminoalcohols. It turned out that the crucial step of the reaction sequence is the final cyclisation of the initially formed N-(2-hydroxyethyl)carboxamide, and this step is no longer catalysed effectively by the Ti(OiPr)4/ionic liquid system.
On the other hand, good to excellent yields were obtained in the synthesis of pyrroles from a 1,4-diketone and sterically less encumbered primary amines (Paal–Knorr synthesis), and for the related pyrazole synthesis from acetylacetone and phenylhydrazine. Here again, the easy recovery and effective reusability of the Ti(OiPr)4/IL system deserve particular notice.
Rigorously dried organic solvents were used. All amines were dried with KOH pellets and distilled prior to use. Lithium bis(trifluoromethylsulfonyl)imide (99%) was purchased from Acros Organics or IoLiTec GmbH.
The guanidinium triflates 1a and 1b were obtained chloride-free from the corresponding ureas and amines according to the literature.25 Guanidinium bis(triflamides) 2a, 2b, 2c and 2f and guanidinium dicyanamide 3a were obtained from the corresponding hexaalkylguanidinium chlorides by anion exchange reactions as reported.24,73,74 The hexaalkylguanidinium chlorides in turn were prepared from N,N,N′,N′-tetraalkyl(chloro)formamidinium chlorides by an adaptation of the classical procedure.26,73,74 The corresponding chloride required for the synthesis of bis(triflamide) 2f was obtained from phosgene iminium chloride and dihexylamine.24 1-Butyl-3-methylimidazolium (BMIm) bis(triflamide) and n-hexyltrimethylammonium bis(triflamide) were obtained from the corresponding chlorides by anion exchange. N-Hexyltrimethylammonium iodide ([Me3HexN]I), used as a precursor for [Me3HexN]NTf2, was prepared according to MacFarlane et al.75
The NMR data of the synthesised lactams, amides, oxazolines, pyrroles, and pyrazoles were in agreement with data in the literature. The purity of the obtained products was confirmed by elemental analyses.76.77
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