Anil Kumar
Mutyala
and
Nitin T.
Patil
*
Division of Organic Chemistry, CSIR – National Chemical Laboratory, Dr. Homi Bhabha Road, Pune 411 008, India. E-mail: n.patil@ncl.res.in
First published on 25th March 2014
This highlight describes the synthesis and catalytic activities of heterogeneous chiral Brønsted acid catalysts. The heterogeneous catalysts are stable, easily separable from the reaction mixture and can be used multiple times without any loss of activity. As a remarkable particularity, the use of heterogeneous catalyst systems has been exemplified for designing continuous flow reactors.
In 2010, a research group of Rueping in collaboration with Sugiono reported the first example of immobilization of a chiral Brønsted acid onto a polymer network.3 The polymer-bound Brønsted acid catalyst can not only be easily recovered from the reaction mixture but it can also be easily reused in several catalytic cycles without any loss of reactivity and selectivity. The heterogeneous catalysts 2 and 4 were prepared by cross-linking radical polymerization with styrene and divinylbenzene from catalysts 1 and 3, respectively (Scheme 1). The catalytic ability of the polymer-supported catalysts 2 and 4 was subsequently evaluated in transfer hydrogenations of quinolines (5a→6a) and benzoxazines (8→9) as depicted in Schemes 2 and 3, respectively. It was found that the catalytic activities and the asymmetric induction are comparable to those of the homogeneous reactions demonstrating the efficiency of this new catalyst system. It is noteworthy that the catalysts 2 and 4 are in the form of polymer-stick and therefore after completion of the reaction the separation of the catalyst can be simply achieved by pulling the stick from the reaction mixture. The polymer stick was successfully recycled and reused for 12 cycles without any loss of activity (Scheme 3).
In general, the bulky nature of the substituents at the 3,3′ position of BINOL derived phosphoric acid is crucial for obtaining high enantioselectivity.1 This reason could be attributed to the increase in rigidity of the catalyst structure which in turn develops a rigid chiral pocket which is necessary for enantioselective induction. The heterogeneous catalysts 2 and 4 developed by Rueping/Sugiono also bear bulky substituents at the 3,3′ position. In the case of catalyst 2, the polymer is providing the steric hindrance; whereas, in the case of catalyst 4 the steric hindrance is already embedded in the monomer and the polymer chain is located far away from the active sites.
Very recently, collaborative efforts of the research group of Thomas and Blechert revealed a new chiral microporous recyclable heterogeneous catalyst made from a BINOL-derived phosphoric acid (BNPPA).4 The first step in preparation of the catalyst was the Suzuki coupling reaction between diboronic acid 10 and 3-(10-bromoanthracen-9-yl)-thiophene 11 to give 12 in good yield. Subsequent demethylation with BBr3 followed by treatment with POCl3 gave BNPPA chloride 13 which on hydrolysis with aq. HCl afforded the desired product 14. However, this monomer 14 turned out not to be suitable for oxidative coupling owing to solubility issues. Incidentally, the FeCl3-mediated oxidative polymerization reaction was successful with the highly soluble 13 affording the polymeric acid chloride 15. Hydrolysis of 15 with aq. HCl and multiple washing with ethanol, THF, and CHCl3 gave the desired product 16 as a powder, which was found to be insoluble in solvents such as EtOH, THF, CHCl3 and CH2Cl2 (Scheme 4).
The BNPPA derived heterogeneous catalyst with high permanent surface area was found to be highly active and selective in enantioselective organocatalysis. For instance, transfer hydrogenation of 3-phenyl-2H-1,4-benzoxazine has been performed with catalysts 14 and 16 (Scheme 5). The enantioselectivity was found to be 99% when 14 was used; and the use of the polymeric network 16 afforded a product with an ee of 98%. The result clearly shows that nearly no loss in ee occurred when switched over to heterogeneous catalysis. The heterogeneous catalyst 16 was easily separated by centrifugation and reused for further repeating runs. For each run, 99% conversion and 98% ee were observed and even after 10 runs, the catalyst works without any loss in activity or enantioselectivity (Scheme 5).
Not only benzoxazines but also quinolines were found to be hydrogenated under the established heterogeneous conditions. For instance, the asymmetric transfer hydrogenation reaction of 2-arylquinolines was carried out with the polymer network 16 (5→6) and the results showed that the performance of the polymer network is comparable to the homogeneous reaction and gives high ee's for different aryl substituents (Scheme 6).
It must be noted that the Rueping/Sugiono catalyst 4 requires 20–24 h time to achieve full conversion with 94% ee for asymmetric hydrogenation of 8 (Scheme 3) and the Thomas/Blechert catalyst 16 catalyzes the same reaction just in 2 h with enhanced enantioselectivity (Scheme 5). The reaction rate with the heterogeneous catalyst 16 was also monitored by kinetic experiments and found to be as fast as with the homogeneous catalyst 14 owing to its microporous nature and high surface area (Schemes 5 and 6). The heterogeneous catalyst 16 can be easily separated by centrifugation and reused for several runs without any loss in activity or selectivity. The authors performed hot extraction experiments to check whether the catalysis is truly heterogeneous in nature or not. After 50% conversion of substrate 8, they filtered out catalyst 16, and even after 24 h they observed no further conversion of substrate 8 to the product confirming that the catalysis is truly heterogeneous.
As shown in Scheme 7, the BNPPA-derived catalyst 16 can also be used for the asymmetric Friedel–Crafts alkylation of unprotected pyrroles with nitroalkenes. The reaction in a mixture of DCM and toluene at room temperature afforded a yield of 91% with a selectivity of 96% ee. The heterogeneous catalyst 16 is also very useful in catalyzing an aza-ene-type reaction between (N-(1-(4-bromophenyl)vinyl)acetamide) 18 and (E)-N-benzylidenebenzamide to give the corresponding adduct which on subsequent hydrolysis afforded the β-amino ketone 19 in 82% yield and 81% ee.
Very recently, Pericàs and coworkers designed polystyrene-supported chiral BINOL derived phosphoric acid.5 As outlined in Scheme 8, it is evident that the immobilization was done at the remote position to avoid perturbation of the active site of the catalyst. The synthesis began with the readily available 6-hydroxymethyl (R)-BINOL derivative 20. Compound 20 was converted to the 6-hydroxymethyl derivative 22 in four steps (cf. 21) and, subsequently, this monomer was anchored onto a Merrifield resin by nucleophilic substitution of chlorine atoms (cf. 23). The desired heterogeneous catalyst 24 was obtained after cleavage of the -MOM group and subsequent phosphoric acid formation followed by HCl wash.6
The immobilized catalyst 24 was found to be highly active for the enantioselective Friedel–Crafts reaction of indoles and sulfonylimine to afford 3-indolylmethanamines in high yields and excellent ee's (Scheme 9). It is interesting to note that the results obtained with this catalyst were comparable to those reported by You and co-workers with a homogeneous Brønsted acid catalyst.7 The report by Pericàs and coworkers clearly demonstrates two striking observations over the superiority of heterogeneous catalysts to homogeneous catalysts: (1) with the PS-supported catalyst 24, good ee's were obtained at room temperature and there is no need of cooling the reaction mixture at –68 °C; (2) the reaction works well only with 1.5 equivalents of indole and a large amount of indole is not necessary.
Scheme 9 Enantioselective Friedel–Crafts reaction of indoles and sulfonylimine catalysed by the PS-supported chiral Brønsted acid 24. |
The catalyst proved to be recyclable up to six cycles without a drop of yield and ee. However, a small drop in ee was observed in the seventh cycle. Very interestingly, the authors found that the activity of the catalyst could be regained with a simple acidic wash (HCl in EtOAc) of the catalyst. Notably, the reactivated catalyst was even more active than the initial one, which allowed for seven more cycles without any significant loss in activity or ee. This observation could be attributed to the presence of phosphate salt that remained during HCl work up in the final stage of phosphoric acid preparation.6 Thus, the authors decided to use HCl/EtOAc washings as the last stage of the preparation of 24.
The research group of Pericàs further endeavoured to use the PS-supported catalyst 24 for designing a single-pass, continuous flow reactor.8 It should be noted that the use of a chiral Brønsted acid in designing a continuous flow micro-reactor was shown for the first time by Rueping et al.9 However, in this case the monomeric catalyst was pumped into the solution and thus the advantages of a supported catalyst could not be fully exploited. With Pericàs's continuous flow reactor, N-Ts imine derived from tosylimine and p-tolualdehyde, reacted with indole to obtain corresponding product in 80% yield and 94% ee.
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