ChemComm
Communication
Scheme 4 Optimization of the benzoylation of ouabagenin derivative 9.
in the formation of the monobenzoylated sugar 6a while mixtures these exact reaction conditions with DMAP, instead of the
with 6b and 6c were obtained through the use of other catalysts. substrate-optimized catalyst, the dibenzoylated product 10c
When using DMAP under solution conditions for the benzoylation was found to be the sole product of the reaction.
of diol 7, a compound closely similar to 5 but with an additional
In summary, we have presented how acylation reactions
ether group, we only obtained the dibenzoylated product 8c, catalyzed by solid-supported derivatives of DMAP can be opti-
presumably due to the low solubility of the starting diol 7 under mized with the goal to achieve increased site-selectivity in the
the reaction conditions, compared to an enhanced solubility of reactions. The catalysts consist of a catalytically active DMAP
the mono- and dibenzoylated compounds 8 (Scheme 3b). On the unit and vary in a peptide chain. The catalysts that were found to
other hand, the use of the supported catalysts allowed for the be optimal for a particular substrate can be recovered and reused
straightforward formation of the monobenzoylated compounds while maintaining both their activity and selectivity; a library
and underlines the hypothesis that the solid support is not once created can be used for screening purposes in a continuous
an innocent bystander; instead, the resin may influence the way. As a result, the use of the solid-supported catalysts is
substrate-specificity through, for example, polarity and diffusion significantly more cost-effective than using the related DMAP–
effects. We optimized the benzoylation of diol 7 with the solid- peptide conjugates not attached to the solid support.
supported catalysts and found that Ac-Phe-Asp-Gln-Thr-Val-1-
Ala-His-resin and Ac-1-Gln-Ala-Phe-Val-Leu-Lys-Ser-resin performed
equally well: the monobenzoylated compound 8a was obtained
as the exclusive product. This result highlights how fully unequal
peptide sequences can afford the same selectivity effect while
Notes and references
1 (a) M. Reetz, J. Am. Chem. Soc., 2013, 135, 12480; (b) R. Breslow,
Artificial Enzymes, Wiley-VCH, Weinheim, 2005; (c) C. M. Clouthierab
and J. N. Pelletier, Chem. Soc. Rev., 2012, 41, 1585.
others (e.g., Ac-Pro-Ala-Leu-Val-Thr-1-resin) are less effective and
provide product mixtures.
2 I. S. Young and P. S. Baran, Nat. Chem., 2009, 1, 193.
3 (a) X. Zhu and R. R. Schmidt, Angew. Chem., Int. Ed., 2009, 48, 1900;
(b) D. Lee and M. S. Taylor, Synthesis, 2012, 3421.
4 M. C. White, Synlett, 2012, 2746.
As a second case study, we chose the benzoylation of ouabagenin-
derived acetonide 9.21 As summarized in Scheme 4, the optimization
of this reaction was also successful: an excellent selectivity for the
monobenzoylate compound 10a was found when employing Ac-Val-
1-Phe-Pro-Ala-Leu-Lys-resin. In the presence of Ac-Thr-Lys-1-His-Leu-
Val-Ala-resin, for example, significant amounts of compound 10b
were generated. We then focused on the preparative scale benzoyla-
tion of the ouabagenin derivative 9. Using the optimized catalyst
Ac-Val-1-Phe-Pro-Ala-Leu-Lys-resin, the reaction was run until
complete conversion with a large excess of both benzoic acid
anhydride (15 equivalents) and triethylamine (20 equivalents) at
room temperature in DMF. The desired product of the mono-
benzoylation, i.e. 10a, was isolated in 80% yield; and after the
reaction, the catalyst was entirely recovered. For a subsequent
recycling study, the benzoylation of 9 was performed under the
same reaction conditions as described above, except for the use
of the recovered Ac-Val-1-Phe-Pro-Ala-Leu-Lys-resin catalyst. It
was of utmost importance that the resin, after recovery through
filtration, was carefully washed with CH2Cl2–MeOH (95/5) con-
taining 3% triethylamine. Up to eleven successive runs were
tested, and the product yield for each run was similar to that
found for the first run, thus demonstrating the good reusability
of the solid catalysts in the liquid phase.22 We note that under
5 J. L. Jeffrey, J. A. Terrett and D. W. C. MacMillan, Science, 2015,
349, 1532.
¨
6 (a) M. Jager and A. J. Minnaard, Chem. Commun., 2016, 52, 656; (b) P. A.
Jordan and S. J. Miller, Angew. Chem., Int. Ed., 2012, 51, 2907;
(c) K. Chung and R. M. Waymouth, ACS Catal., 2016, 6, 4653;
(d) N. N. H. M. Eisink, J. Lohse, M. D. Witte and A. J. Minnaard, Org.
Biomol. Chem., 2016, 14, 4859.
7 (a) M. S. Taylor, Acc. Chem. Res., 2015, 48, 295; (b) M. G. Chudzinski,
Y. Chi and M. S. Taylor, Aust. J. Chem., 2011, 64, 1466; (c) D. Lee and
´
M. S. Taylor, Org. Biomol. Chem., 2013, 11, 5409; (d) E. Dimitrijevic
and M. S. Taylor, Chem. Sci., 2013, 4, 3298; (e) D. Lee and
M. S. Taylor, J. Am. Chem. Soc., 2011, 133, 3724; ( f ) K. Tanveer,
K. Jarrah and M. S. Taylor, Org. Lett., 2015, 17, 3482; (g) G. E. Garrett,
K. Tanveer and M. S. Taylor, J. Org. Chem., 2017, 82, 1085.
8 (a) Z. X. Giustra and K. L. Tan, Chem. Commun., 2013, 49, 4370;
(b) Y. Lu, C. Hou, J. Ren, X. Xin, H. Xu, Y. Pei, H. Dong and Z. Pei,
Molecules, 2016, 21, 641; (c) A. D. Worthy, X. Sun and K. L. Tan,
J. Am. Chem. Soc., 2012, 134, 7321; (d) X. Sun, H. Lee and K. L. Tan,
Nat. Chem., 2013, 5, 790.
9 (a) K. Sakurai, T. Takeshita, M. Hiraizumi and R. Yamada, Org. Lett.,
2014, 16, 6318; (b) Y. Ueda, W. Muramatsu, K. Mishiro, T. Furuta
and T. Kawabata, J. Org. Chem., 2009, 74, 8802; (c) B. Ren, M. Rahm,
X. Zhang, Y. Zhou and H. Dong, J. Org. Chem., 2014, 79, 8134;
(d) I.-H. Chen, K. G. M. Kou, D. N. Le, C. M. Rathbun and V. M. Dong,
Chem. – Eur. J., 2014, 20, 5013; (e) C. L. Allen and S. J. Miller, Org. Lett.,
2013, 15, 6178; ( f ) F. Iwasaki, T. Maki, O. Onomura, W. Nakashima
and Y. Matsumura, J. Org. Chem., 2000, 65, 996; (g) Y. Demizu,
Y. Kubo, H. Myoshi, T. Maki, Y. Matsumura, N. Moriyama and
O. Onomura, Org. Lett., 2008, 10, 5075; (h) W. Muramatsu and
This journal is ©The Royal Society of Chemistry 2017
Chem. Commun.