Hai Anh Le Phuong‡
a,
Levente Cseri‡a,
George F. S. Whiteheadb,
Arthur Garfortha,
Peter Buddb and
Gyorgy Szekely*a
aSchool of Chemical Engineering & Analytical Science, The University of Manchester, The Mill, Sackville Street, Manchester, M1 3BB, UK. E-mail: gyorgy.szekely@manchester.ac.uk; Tel: +44 (0)161 306 4366
bSchool of Chemistry, The University of Manchester, Oxford Road, Manchester, M13 9PL, UK
First published on 20th November 2017
2-Imidazolines are heterocycles with a wide range of applications in biomedical science, pharmaceuticals, surfactants and catalysis. The 2,4,5-trisubstituted derivatives are conventionally prepared through the reaction of aromatic aldehydes and ammonia, requiring harsh conditions and toxic solvents. Herein, we report a sustainable, one-pot synthetic route to obtain cis or trans diastereomers of 2,4,5-trisubstituted-2-imidazolines. The reaction parameters, such as the ammonia source, the substituents of the aromatic aldehydes and the effect of temperature and solvent, were systematically explored. The synthesis was attempted in sixteen different green solvents. Reaction kinetics and quantum mechanical studies (DFT B3LYP/6-31G(d,p)) revealed the elementary steps of the cyclisation and refuted two common speculations. The limitations of the synthesis were explored through varying the p-, o-, and m-substituents on the aldehyde as well as employing heterocyclic and non-aromatic derivatives. Ten out of the twelve products synthesised in this work can be solely purified by crystallisation, without the need for extraction or chromatography. Owing to the bulky nature of the products, the applicability of membrane-based purification was demonstrated to further improve the sustainability of the synthesis.
The reported syntheses for obtaining 2,4,5-trisubstituted-2-imidazolines are summarised in Table 1. 2,4,5-Trisubstituted-2-imidazolines were successfully synthesised from benzylamine and carbon tetrachloride,14 and 1,2-cyclic sulphates and amidine.15 However, none of these syntheses were as prominent as the reaction from benzaldehyde and ammonia.16 Benzaldehyde reacts with liquid ammonia to produce hydrobenzamide (also known as 1,3,5-triaryl-2,4-diazapentadiene), an intermediate which upon heating or employing strong base deprotonates and subsequently forms amarine, supposedly via disrotatory pericyclic closure.11,17 The rate of pericyclisation usually depends on both the steric and electronic character of the substituents.18 However, the effect of substituents on the synthesis of 2-imidazolines and the reaction mechanism have yet to be investigated.
Reactants | T (°C) | Solvent | Additives | Purification | Yield (%) | Ref. |
---|---|---|---|---|---|---|
a Two-step reaction. The 2,4-diazapentadiene intermediate was isolated via recrystallisation from cyclohexane. The 2-imidazoline product was purified by recrystallisation from petroleum ether. | ||||||
Benzylamine & carbon tetrachloride | 125 | Carbon tetrachloride | Cu, Fe catalyst | Column chromatography | 1–24 | 14 |
1,2-Cyclic sulphates & amidine | 85–162 (reflux) | Dimethoxyethane/Methoxyethyl ether | — | Extraction | 22–64 | 15 |
Benzaldehyde & ammoniaa | 130 | Benzene | — | Recrystallisation | 81 | 12 |
Benzaldehyde & HDMS | 120 | — | — | Column chromatography | 47–89 | 19 |
Benzaldehyde & urea | 120 | DMF | Cs2CO3 | Column chromatography | 40–79 | 20 |
Notwithstanding the moderate to good yields, most reactions require additives, extensive purification, or harsh conditions, i.e., high temperature, toxic or banned solvents. In addition, additives and catalysts were usually used for the preparation of the desired product, which results in additional waste that has to be managed. While attempts have been made towards a more sustainable synthesis of 2,4,5-trisubstituted-2-imidazolines, there is a need for exploring green solvents and purification processes.
The 21st century's sustainability grand challenge requires the chemical industry to employ mild reaction conditions, and non-toxic, non-flammable chemicals and solvents, with the aim of minimising environmental impact.21 Solvents for reaction and purification account for more than 80% of the total mass used for the production of pharmaceuticals,22 and consume 60% of the total energy.23 The solvent selection guides established by pharmaceutical companies provide practical advice to reduce the environmental burden associated with solvent usage.24,25 Following the guidelines, sixteen different green solvents were screened for the syntheses presented in this work. As an effective process intensification tool due to the mild conditions and low energy consumption,26 membrane technology is a sustainable alternative to conventional purification techniques such as crystallisation and chromatography,27 which can be more easily implemented in continuous processing.28 Consequently, the potential of membrane-based purification of the 2-imidazoline products was evaluated.
Herein, we report the development toward an environmentally benign, diastereoselective, one-pot synthesis of 2,4,5-trisubstituted-2-imidazolines employing non-toxic ammonium salts, green solvents and purification. The kinetics and reaction mechanism were explored to reveal the governing factors of the pericyclisation. To the best of our knowledge the kinetic studies and quantum mechanical calculations for the reaction of aldehyde and ammonia to produce 2,4,5-trisubstituted-2-imidazolines have not yet been reported.
Entry | Solvent | T (°C) | Yieldb (%) |
---|---|---|---|
a The reactions were carried out with 4-(trifluoromethyl)benzaldehyde (3 mmol), (NH4)2CO3 (6 mmol), and solvent (6 mL) for 96 h.b Isolated yield.c The reaction was performed for 24 h at which point product formation stopped according to HPLC monitoring. | |||
1 | 2-MeTHF | 20 | 21 |
2 | 2-MeTHF | 30 | 40 |
3 | 2-MeTHF | 40 | 67 |
4 | 2-MeTHF | 50 | 48 |
5 | Ethyl lactate | 40 | 66 |
6 | Propylene carbonate | 40 | 66 |
7 | Sulfolane | 40 | 65 |
8 | 2-Propanol | 40 | 55 |
9 | Methanol | 40 | 41 |
10 | DMSOc | 40 | 38 |
11 | MTBE | 40 | 22 |
12 | CPME | 40 | 11 |
13 | 1-Butanol | 40 | 10 |
14 | Butyl acetate | 40 | 6 |
15 | Dimethyl carbonate | 40 | 2 |
16 | Water | 40 | 1 |
To study the effect of ammonia sources (2 eq.) on the reaction, non-toxic ammonium salts of acids covering a wide range of pKa values (−6.30 to 10.32) were selected (Table 3). The highest conversion was achieved using (NH4)2CO3 (entry 1), while moderate and poor yield was obtained with NH4HCO3 and NH4OAc (entries 2 and 3), respectively. NH4HCOO (entry 4) did not provide the desired product at 40 °C, but a moderate yield was obtained at the reflux temperature of 81 °C. Moderate yield was also achieved using NH4CF3COO at reflux (entry 5). In contrast, no product was formed with NH4Cl (entry 6) under reflux conditions. These results suggest that employing the ammonium salt of a weaker acid (therefore with higher pKa value) leads to increased reaction rate due to the more favoured dissociation of the salt and the more basic environment. In addition, the amount of ammonia source was also investigated (entry 1). The increase of ammonium carbonate from 1 to 2 eq. led to 23% yield enhancement. However, further increase to 4 eq. did not result in significant improvement.
Entry | NH3 source | pKa of acid31 | T (°C) | Yieldb (%) |
---|---|---|---|---|
a The reactions were carried out with 4-(trifluoromethyl)benzaldehyde (3 mmol), ammonium salt (6 mmol), and 2-MeTHF (6 mL) for 96 h.b Isolated yield.c 1 eq. ammonium salt (3 mmol) was used.d 4 eq. ammonium salt (12 mmol) was used.e Instead of 40 °C the reaction was performed at 35 °C due to the decomposition of NH4HCO3 at 40 °C.32 | ||||
1 | (NH4)2CO3 | 10.32 | 40 | 44c/67/71d |
2 | NH4HCO3 | 6.37 | 35e | 42 |
3 | NH4OAc | 4.75 | 40 | 11 |
4 | NH4HCOO | 3.75 | 40/reflux | —/48 |
5 | NH4CF3COO | 0.23 | reflux | 44 |
6 | NH4Cl | −6.30 | reflux | — |
The effect of both electron withdrawing and electron donating p-substituents on the reaction were systematically investigated (Table 4). Substrates with strongly or moderately electron-withdrawing groups (EWG) (entries 1–7), i.e., moderate to high Hammett sigma constants (σ = 0.45–0.82), provided the desired product in good to excellent yield. The substrate with weakly electron-withdrawing bromide group (entry 8; σ = 0.23) only afforded the 2-imidazoline derivative in poor yield. Reactions with non-EWGs (–H, –OH) were attempted but did not yield the imidazoline products.
Entry | R | σb (−) | t (h) | Yieldc (%) | Product |
---|---|---|---|---|---|
a Unless otherwise noted, the reaction was performed with p-substituted benzaldehyde (3 mmol), (NH4)2CO3 (6 mmol), and 2-MeTHF (6 mL) at 40 °C.b Hammett sigma constant.33c Isolated yield.d Due to the poor substrate solubility in pure 2-MeTHF, the reaction required the use of 2-MeTHF (5 mL) and DMSO (1 mL) solvent mixture.e The lower 58% isolated yield is a result of excessive by-product formation when (NH4)2CO3 (6 mmol) was used, while the higher 85% isolated yield was obtained with the use of NH4OAc (6 mmol) ammonia source. This result implies that 3 is sensitive to oxidation under basic conditions. | |||||
1 | –NMe3+I−d | 0.82 | 24 | 83 | 2 |
2 | –NO2e | 0.78 | 24 | 58/85 | 3 |
3 | –SO2Med | 0.72 | 48 | 69 | 4 |
4 | –SF5 | 0.68 | 36 | 87 | 5 |
5 | –CN | 0.66 | 96 | 68 | 6 |
6 | –CF3 | 0.54 | 96 | 67 | 1 |
7 | –COOMe | 0.45 | 96 | 65 | 7 |
8 | –Br | 0.23 | 168 | 8 | 8 |
9 | –H | 0.00 | 168 | — | — |
In order to further explore the effect of EWGs on the reaction rate, the kinetics of the reaction was studied. The reactions of (NH4)2CO3 with 4-nitrobenzaldehyde, 4-(pentafluorosulfanyl)-benzaldehyde, 4-(trifluoromethyl)benzaldehyde, and methyl 4-formyl benzoate were chosen as model systems because they provided the desired product under the same conditions with a considerable yield, and they cover a wide range of σ (0.45–0.78). A consecutive reaction, 3A → B → C, was suggested for the reaction kinetics based on the formation of stable intermediate B identified as hydrobenzamide in the literature.11 In order to obtain the reaction rate constants k1 and k2, the rate eqn (1)–(3) have to be solved.
(1) |
(2) |
(3) |
Fig. 2 Substrate conversion profile as a function of reaction time. Symbols denote the experimental data, while the lines signify the calculated plots. |
In order to investigate the relationship between the reaction rates and the electron-withdrawing substituents, the calculated k1 and k2 values are displayed as a function of the σ in Fig. 3a. Although increasing rate constants for both k1 and k2 were expected with increasing σ no direct relationship between the three constants was found. The rate of hydrobenzamide formation increases from σ = 0.45 (–COOMe) until σ = 0.68 (–SF5), however, k1 significantly drops at σ = 0.78. The rate constant of the intramolecular ring closure decreases between σ = 0.45 (–COOMe) and σ = 0.54 (–CF3) and then grows with increasing electron-withdrawing property. These results could be the consequence of other factors, such as low solubility of the intermediate.
Fig. 3 The k1 and k2 reaction rate constants (a), and the relative Gibbs free energy of the B → C reaction (ΔGr) and the deprotonation step (ΔGdeprot) (b) as a function of Hammett sigma constant (σ). |
Density functional theory computational analysis (DFT B3LYP/6-31G(d,p)) revealed the cyclisation mechanism of 1 from the hydrobenzamide intermediate (1hb) (Fig. 4). The deprotonation of 1hb forms a high energy carbanion intermediate (1cU), which stabilises by the translation of the ammonium counter ion. Subsequent protonation of 1cU on its nitrogen atom results in 1zw zwitterionic intermediate, which provides 1 via ring closure. The Gibbs free energy of both the cyclisation (ΔGr) and the deprotonation (ΔGdeprot) was derived for substituents with different electron-withdrawing properties (different σ values). The dependence of ΔGr on σ is negligible; however, the ΔGdeprot values significantly decrease with higher σ values (Fig. 3b). Consequently, the reaction favours EWGs, which is in line with the experimental observations (see Table 4).
Fig. 4 Computed relative Gibbs free energy profile of hydrobenzamide cyclisation in the presence of ammonia. |
The DFT results refuted two speculations about the mechanism of the cyclisation. First, the cyclisation from the carbanion species with electron-withdrawing substituents is not favourable thermodynamically (Table S2, ESI†), despite speculations that the reaction proceeds with the ring closure of the carbanion intermediate leading to the negatively charged imidazoline which is the deprotonated form of 2-imidazoline (Scheme S1a, ESI†).11 Second, 1cU is the energetically most favoured carbanion conformer (Table 5). Despite speculations that 1cW has the lowest energy due to the lack of steric hindrance between H(4) and H(5)16 1cU has a quasi-planar structure, which allows the conjugation of the π system to be extended to the whole molecule. However, the steric repulsion between the H(5) and H(34) atoms in 1cS and 1cW forces the ring to turn out of the plane, which decreases the conjugation. The cyclisation was further studied using nuclear independent chemical shift (NICS) calculations.34 NICS(0) values of −1.94 and −3.55 ppm were obtained for the five-membered rings in 1zw and 1, respectively. These relatively small negative NICS(0) values revealed the non-aromatic nature of the rings. In contrast, the large negative NICS(0) value of −11.34 ppm for 1TS-IV proved the aromaticity of the transition state, and consequently, the pericyclic nature of the reaction. The lobes in the highest occupied molecular orbital (HOMO) of 1zw indicate that the cyclisation is allowed progress only in disrotatory mode leading to the cis product (1) according to the Woodward–Hoffman rule.35 The experimental results are in good agreement with the calculations because for all substrates, the formation of solely the cis product was observed. The stereochemistry of 1 (Fig. 5a), 2, and 5 (Fig. S115 and S116, ESI†) was confirmed by single-crystal X-ray diffraction. The stereochemistry of 3, 4 and 6–8 was deduced to be cis as the synthetic methods were identical. This deduction was further supported by the high coupling constants (10.9–11.2 Hz) for the imidazoline hydrogens in the NMR spectra.
As a consequence of the electrocyclic nature of the reaction, the diastereoselectivity can be influenced by the method of reaction initiation. Photoirradiation at 254 nm and 365 nm for 96 h resulted in 39% and 13% conversion with trans:cis product ratio of 1.42 and 1.61, respectively (Scheme 1).
Furthermore, the thermodynamically favoured trans 9 can be selectively obtained by alkali treatment of the cis isomer, similarly to a previously described procedure.13 The trans stereochemistry of 9 (Fig. 5b) was indicated by the lower coupling constant of imidazoline hydrogens (J = 8.8 Hz) compared to the case of 1 (J = 10.9 Hz).
Besides p-substituted aldehydes, the synthesis was also performed from o-, and m-substituted aldehydes, in order to investigate the effect of the substituent position on the reaction (Table 6). Moreover, attempts were made to expand the substrate scope to heterocyclic and non-aromatic aldehydes as well. Comparing the position of substituents (entries 1–2), the m-substitution provided the desired product in good yield, but the reaction was slower compared to the p-substituted analogue. The o-substitution did not afford the imidazoline product as a consequence of steric effects, i.e., the close proximity of the bulky –CF3 substituent to the formyl group sterically hinders the reaction. When it was attempted to produce the product from 4-pyridinecarboxaldehyde and (NH4)2CO3 with the optimised conditions, a product mixture of imidazoline and imidazole (1:1) was obtained. However, when NH4OAc was used as ammonia source, the desired 2-imidazoline product was isolated in a good yield of 72%. This result suggests that, similarly to 3, product 11 is also sensitive to oxidation under basic conditions. The synthesis of 12 was performed using trans-cinnamaldehyde and (NH4)2CO3 as shown in entry 4 in Table 6. The reaction provided the product in good yield within 24 h, which indicates that highly conjugated aldehydes also afford the desired 2-imidazoline product. Therefore, the reaction was also attempted using ethyl 4-oxobut-2-enoate as a non-aromatic starting material. Similarly to trans-cinnamaldehyde, the consumption of starting material was virtually 100% within 24 h (entry 5). The reaction, however, did not stop at the 2-imidazoline product, but through an intramolecular double bond migration a trisubstituted imidazole product was formed instead. Consequently, it could be concluded that a conjugated system which is sterically unhindered is required for the presented synthetic methodology to yield 2-imidazolines.
Entry | R–CHO | Time (h) | Yieldb (%) | Product |
---|---|---|---|---|
a The reactions were performed with aldehyde (3 mmol), (NH4)2CO3 (6 mmol), and 2-MeTHF (6 mL) at 40 °C.b Isolated yield.c The ammonia source was NH4OAc (6 mmol).d Formation of the desired 2-imidazoline was not observed, but 13 was obtained instead. | ||||
1 | 128 | — | — | |
2 | 128 | 61 | 10 | |
3 | 36 | 72 | 11 | |
4 | 24 | 84 | 12 | |
5 | 24 | 71d | 13 |
Most green chemistry articles solely focus on improving the synthetic step without considering the purification and isolation of the product. In order to address the inherent environmental burden of downstream processing, the isolation of the 2-imidazoline products was aimed to be performed in a single crystallisation step employing a green solvent, which eliminated the use of tedious chromatography employed in previous procedures (see Table 1). Furthermore, the considerable increase in molecular size during the reaction allowed the use of solvent-resistant nanofiltration for product purification. Four membranes, namely GMT-oNF-1, GMT-oNF-2, NF030306, and Duramem 300, were screened at 10–40 bar pressure to obtain solvent flux and solute rejection for product 1, and the corresponding benzaldehyde substrate impurity (Fig. 6a). Flux is defined as volume of solvent that permeates the membrane per unit area in a given time, while rejection is the ratio of solute concentration in the permeate and the retentate. Permeance is defined as the flux normalised by the applied pressure. The permeances (expressed in L m−2 h−1 bar−1) obtained for GMT-ONF-1, GMT-ONF-2, NF030306, and Duramem 300 were 4.39 ± 0.6, 5.2 ± 0.6, 0.35 ± 0.04, and 0.26 ± 0.01, respectively. Despite the relatively low permeance obtained for Duramem 300, it showed excellent product rejection above 99%.
The concentration and purity profiles for single-stage and two-stage diafiltration are shown in Fig. 6b. The detailed description of the mathematical framework can be found in the ESI.† The number of diavolumes is a time-like parameter indicating the progress of the filtration and it is defined as the ratio of permeate and retentate volume. The number of diavolumes required to obtain 99% product purity with a single-stage and two-stage diafiltration is 5 and 6, respectively (see dotted lines). In line with expectations,36 the two-stage cascade configuration markedly improved the product yield from 95% to 99.8%. The purification of a post-reaction mixture validated the calculated model. During the process, Duramem 300 at 20 bar demonstrated stable permeance and rejection performance over 8 days of continuous operation in 2-MeTHF (Fig. S118, ESI†). The solvent consumption of the filtration could be minimised by implementing an additional filtration stage for in situ solvent recovery.28,37
NF010206 membrane was purchased from Solsep BV (Apeldoorn, Netherlands); GMT-oNF-1 and GMT-oNF-2 were purchased from Borsig Membrane Technology GmbH (Gladbeck, Germany); and Duramem 300 was obtained from Evonik-MET (Essen, Germany).
The products were characterised by IR, 1H NMR, 13C NMR, 19F NMR, 1H COSY, 1H–13C HMBC and 1H–13C HSQC, mass spectrometry (MS) and, where possible, single-crystal XRD measurements. IR spectra were recorded from dry samples using a Thermo Fisher Nicolet iS5 iD5 ATR-FTIR spectrometer. NMR analyses were performed on a B500 Bruker Avance II+ 500 MHz instrument. Spectra were processed using the MestReNova software. Low resolution mass spectra were recorded on a Waters SQD2 Single l Quadrupole Mass spectrometer used with a Waters Acquity UHPLC using 100% methanol as mobile phase. Electrospray ionisation technique was used in negative or positive mode. High resolution mass measurements were performed on a Thermo Exactive plus EMR Orbitrap mass spectrometer, used with a Thermo Ultimate 3000 UHPLC using 100% methanol as mobile phase. Single-crystals were grown by slow evaporation at low-temperature (2 °C) from acetonitrile for X-ray analysis. CCDC 1576088 (1), CCDC 1576089 (2), CCDC 1576090 (5) and CCDC 1582071 (9) contain the supplementary crystallographic data for this paper.†
1H NMR (500 MHz, DMSO-d6) δ 8.26 (d, J = 8.8 Hz, 2H), 8.19 (s, 1H) 8.18 (d, J = 9.0 Hz, 2H), 7.65 (d, J = 9.2 Hz, 2H), 7.62 (d, J = 9.3 Hz, 2H), 7.29–6.92 (m, 4H), 5.78 (d, J = 10.9 Hz, 1H), 5.54 (d, J = 10.9 Hz, 1H), 3.69 (s, 9H), 3.47 (s, 18H); 13C NMR (126 MHz, DMSO-d6) δ 162.5, 148.8, 145.8, 145.5, 141.7, 141.7, 131.1, 129.1, 128.9, 128.3, 121.0, 119.4, 119.2, 73.2, 64.0, 56.5, 56.5; IR (ATR-FTIR) νmax 3011 (CH), 1617 (CN), 1468 (C(N)–N), 955, 938 (C–N), 845 (C–N+Me3) cm−1; HRMS (ESI+/Orbitrap) m/z: calcd for [M]3+ C30H42N5: 157.4473; found: 157.4475; D = −1.01 ppm; mp: 168.7–169.4 °C decomp. Yield: 83% (590 mg) following recrystallisation from acetonitrile (5 mL). Product 2 was obtained as white crystals.
1H NMR (500 MHz, DMSO-d6) δ 11.63 (s, 2H), 8.22 (d, J = 8.7 Hz, 2H), 8.00 (d, J = 8.7 Hz, 2H), 7.37 (d, J = 8.5 Hz, 4H), 7.09 (d, J = 8.5 Hz, 4H), 5.98 (s, 2H); 13C NMR (126 MHz, DMSO-d6) δ 165.1, 134.7, 132.9, 131.6, 131.4, 130.4, 129.6, 121.8, 121.7, 64.1; IR (ATR-FTIR) νmax 3315 (NH), 2955 (CH), 1717 (CO), 1708 (CO), 1608 (CN), 1435 (aromatic CC), cm−1; MS (ESI–/SQD2) m/z: 531.1 [M − H]−; MS (ESI+/SQD2) m/z: 473.3 [M + H]+; HRMS (ESI-/Orbitrap) m/z: calcd for [M + Cl]− C21H15N2Br3Cl: 566.8471; found: 566.8479; D = −1.48 ppm; mp: 325–326 °C. Yield: 8% (45 mg). Product 8 was obtained as white crystals.
1H NMR (500 MHz, THF-d8) δ 8.22 (d, J = 8.1 Hz, 2H), 7.81 (d, J = 8.3 Hz, 2H), 7.70 (d, J = 8.2 Hz, 2H), 7.65 (d, J = 8.2 Hz, 2H), 7.58 (d, J = 8.1 Hz, 2H), 7.48 (brs, 1H), 7.47 (d, J = 8.3 Hz, 2H), 5.14 (d, J = 8.8 Hz, 1H), 4.81 (dd, J = 8.8 and 2.3 Hz, 1H); 13C NMR (126 MHz, THF-d8) δ 163.2, 149.4 (q, J = 1.3 Hz), 149.2 (q, J = 1.3 Hz), 135.1 (q, J = 1.3 Hz), 133.0 (q, J = 32 Hz), 130.6 (q, J = 32 Hz), 130.1 (q, J = 32 Hz), 129.1, 128.4, 128.1, 126.6 (q, J = 3.9 Hz), 126.2 (q, J = 3.9 Hz), 126.2 (q, J = 3.9 Hz), 125.6 (q, J = 272 Hz), 125.4 (q, J = 272 Hz), 125.2 (q, J = 272 Hz), 81.0, 71.0; 19F NMR (471 MHz, THF-d8) δ −63.1 (s, 3F), −63.2 (s, 3F), −63.6 (s, 3F); IR (ATR-FTIR) νmax 3082 (NH), 1601 (CN), 1485 (aromatic CC), 1324 (C–F), 1162 (C–F), 1067 (C–F) cm−1; MS (ESI–/SQD2) m/z: 501.2 [M−H]−; MS (ESI+/SQD2) m/z: 503.2 [M + H]+; HRMS (ASAP+/Orbitrap) m/z: calcd for [M + H]+ C24H16F9N2: 503.1164; found: 503.1148; D = −3.24 ppm; mp: 283–284 °C. Yield: 72% (108 mg) following recrystallisation from toluene (5 mL). Product 9 was obtained as white crystals.
1H NMR (500 MHz, THF-d8) δ 8.39 (s, 1H), 8.38 (d, J = 7.7 Hz, 1H), 7.86 (d, J = 7.8 Hz, 1H), 7.72 (t, J = 8.0 Hz, 1H), 7.54 (brs, 1H), 7.32–7.22 (m, 6H), 7.22–7.14 (m, 2H), 5.80 (br, 1H), 5.52 (br, 1H); 13C NMR (126 MHz, THF-d8) δ 164.2, 142.2, 132.4, 132.3 (br), 132.2 (q, J = 1.0 Hz), 131.6 (br), 131.5 (q, J = 32 Hz), 130.3, 129.3 (br), 129.0 (br), 128.2 (q, J = 3.8 Hz), 125.6 (br), 125.3 (q, J = 272 Hz), 125.1 (q, J = 4.0 Hz), 124.9 (br), 124.5 (br), 123.9 (br), 75.7, 66.6; 19F NMR (471 MHz, THF-d8) δ −63.4 (s, 3F), −63.6 (s, 3F), −63.7 (s, 3F); IR (ATR-FTIR) νmax 3137 (NH), 1615 (CN), 1114 (aromatic CC), 1326 (C–F), 1160 (C–F), cm−1; HRMS (ESI+/Orbitrap) m/z: calcd for [M + H]+ C24H16F9N2: 503.1164; found: 503.1161; D = −0.65 ppm. Yield: 61% (306 mg). Product 10 was obtained as pale yellow resin.
1H NMR (500 MHz, CD3OD) δ 8.78 (d, J = 6.1 Hz, 2H), 8.24 (d, J = 6.1 Hz, 4H), 7.99 (d, J = 6.2 Hz, 2H), 7.14 (d, J = 6.0 Hz, 4H), 5.80 (br, 1H), 5.64 (br, 1H); 13C NMR (126 MHz, CD3OD) δ 166.2, 151.1, 150.1, 149.7, 138.7, 124.8, 124.2, 123.3, 74.5, 65.7; IR (ATR-FTIR) νmax 3156 (NH), 3033 (CH), 1596 (aromatic CN), 1473 (aromatic CC) cm−1; HRMS (ESI–/Orbitrap) m/z: 300.1248 [M − H]−; HRMS (ESI+/Orbitrap) m/z: calcd for [M + Na]+ C18H15N5Na: 324.1220; found: 324.1210; D = −2.29 ppm; mp: 94.0–95.2 °C decomp. Yield: 72% (218 mg). Product 11 was obtained as white crystals.
1H NMR (500 MHz, DMSO-d6) δ 7.54 (d, J = 15.9 Hz, 1H), 7.40 (d, J = 16.2 Hz, 1H), 7.16 (d, J = 16.2 Hz, 1H), 6.75 (d, J = 15.9 Hz, 1H), 4.23 (q, J = 7.1 Hz, 2H), 4.20 (q, J = 7.1 Hz, 2H), 4.03 (q, J = 7.1 Hz, 2H), 3.03 (t, J = 7.2 Hz, 2H), 2.75 (t, J = 7.2 Hz, 2H), 1.27 (t, J = 7.1 Hz, 3H), 1.26 (t, J = 7.1 Hz, 3H), 1.15 (t, J = 7.1 Hz, 3H); 13C NMR (126 MHz, DMSO-d6) δ 171.4, 165.8, 164.9, 141.8, 138.5, 129.4, 127.9, 126.6, 125.1, 118.3, 60.9, 60.3, 60.2, 32.7, 19.6, 14.2, 14.1, 14.0. IR (ATR-FTIR) νmax 1718 (CO), 1707 (CO), 1655 (imidazolium CC), 1185 (C–C(O)–O) cm−1; MS (ESI-/SQD2) m/z: 363.3 [M − H]−; MS (ESI+/SQD2) m/z: 387.4 [M + Na]+; HRMS (ESI+/Orbitrap) m/z: calcd for [M + Na]− C18H24N2O6Na: 387.1527; found: 387.1515; D = −2.99 ppm; mp: 96.3–97.1 °C decomp. Yield: 71% (285 mg). Product 13 was obtained as white crystals.
(4) |
(5) |
Fig. 7 Schematic process configuration for membrane screening, i.e. determination of solute rejection and flux at 10–40 bar pressure using different membranes. |
Footnotes |
† Electronic supplementary information (ESI) available: Synthetic procedures; 1H NMR, 13C NMR, MS, HRMS, FTIR spectra; HPLC methods, chromatograms, kinetic calculations; DFT computational methods & raw data; single crystal XRD data, membrane separation. CCDC 1576088–1576090, 1582071. For ESI and crystallographic data in CIF or other electronic format see DOI: 10.1039/c7ra11827a |
‡ These authors equally contributed to this work. |
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