ChemComm
Communication
To study the confinement effect of the chiral MOF, the catalytic
In conclusion, we have synthesized two microporous 3D MOFs
performance of the monomer TiL(OBu)2 was also studied. utilizing a pyridine- and carboxylic acid-functionalized Ti(salan)
Thioanisole, methyl p-tolyl sulfide and phenyl benzyl sulfide were ligand. The frameworks were shown to be heterogeneous cata-
oxidized by aqueous H2O2 with 4.5 mol% TiL(OBu)2 as the catalyst lysts for asymmetric oxidation of thioethers to sulfoxides, with
(the same TiL loading as that of the heterogenous system). The improved enantioselectivity relative to the homogeneous catalyst.
conversions are obviously higher than those of the corresponding The ready tunability of such a modular approach based on chiral
heterogeneous systems after 6 h, which afforded 8, 12 and 10% ee for metallosalans promises to lead to a variety of framework materials
sulfoxides with 64, 59 and 58% chemoselectivities, respectively with novel enantioselective functions.
(Table 1, entries 3, 6 and 12). Therefore, the TiL-containing frame-
This work was supported by NSFC-21025103 and the Shanghai
work displayed obviously enhanced enantioselectivities and chemo- Science and Technology Committee (10DJ1400100 and 12XD1406300).
selectivities with respect to its homogeneous catalyst, although the
heterogeneous reaction needs a longer time for diffusion of species
into the porous structure. A careful examination of the crystal
structure of 1 reveals that the channel surfaces are uniformly lined
Notes and references
‡ Crystallographic data for 1: M = 3427.85, orthorhombic, space group
P21212, a = 34.4419(13) Å, b = 16.7622(8) Å, c = 18.4473(8) Å, V =
10650.0(8) Å3, Z = 2, Dc = 1.069 Mg mÀ3, F(000) = 3522, 11 722 unique
(Rint = 0.0894), R1 = 0.0794, wR2 = 0.1873 [I > 2s(I)], GOF = 1.074, Flack
parameter = 0.005(12). 2: M = 3246.95, orthorhombic, space group
P21212, a = 34.0597(5) Å, b = 16.9014(2) Å, c = 18.3315(3) Å, V =
10552.6(3) Å3, Z = 2, Dc = 1.022 Mg mÀ3, F(000) = 3392, 12 261 unique
(Rint = 0.0391), R1 = 0.0984, wR2 = 0.2573 [I > 2s(I)], GOF = 1.084, Flack
parameter = 0.031(13). CCDC 936226 and 936227.
with chiral Ti2L2(m2-O) units with Ti sites pointing to the open
channels, and the shortest Ti–Ti distance of adjacent surfaces in a
channel is 3.599 Å (Fig. S5, ESI†). The increased enantioselectivity and
chemoselectivities may arise from geometrical constraints imposed
by the unique chiral micro-environments around the site-isolated
Ti centers, which may effectively restrict molecular motion, leading to
efficient enantiodiscrimination.3c,12 The turnover frequency (TOF)
of (R)-1 and (R)-TiL is 1.24 and 3.50, 1.26 and 3.46, and 0.75 and
3.24 hÀ1, respectively, for oxidation of thioanisole, methyl p-tolyl
sulfide, and phenyl benzyl sulfide; the lower TOF of (R)-1 is probably
due to the diffusion of substrates in the porous structure, which
makes the access of the substrate to the active site slow.
To probe whether oxidation of the sulfides occurs inside the
chiral pores or on the surface of the solid framework catalyst,
a more sterically bulky substrate, benzyl 2-naphthyl sulfide, was
subjected to the oxidation conditions. Less than 5% conversion
was observed when catalyzed by (R)-1 after 16 h, which was
much lower than 88% conversion obtained using the homo-
geneous TiL catalyst within 6 h (Table 1, entries 13 and 14).
This result suggests that the bulky substrate cannot access the
catalytic Ti sites in the porous structure due to its large
diameter and so the oxidation reaction indeed occurs within
the chiral MOF. This point is also supported by the fact that
ground and unground particles of (R)-1 exhibited similar cata-
lytic performance in oxidation of methyl p-tolyl sulfide (91% vs.
90% and 44% vs. 46%, conversions and enantioselectivities
after 16 hours, respectively).
1 (a) L. J. Murray, M. Dinca and J. R. Long, Chem. Rev., 2009, 38, 1294–1314;
(b) H. Furukawa, N. Ko, Y. B. Go, N. Aratani, S. B. Choi, E. Choi, A. O.
¨
Yazaydin, R. Q. Snurr, M. O’Keeffe, J. Kim and O. M. Yaghi, Science, 2010,
329, 424–428; (c) L. E. Kreno, K. Leong, O. K. Farha, M. Allendorf,
R. P. Van Duyne and J. T. Hupp, Chem. Rev., 2012, 112, 1105–1125;
(d) Y. Cui, Y. Yue, G. Qian and B. Chen, Chem. Rev., 2012, 112, 1126–1162;
(e) H. Wu, Q. Gong, D. H. Olson and J. Li, Chem. Rev., 2012, 112, 836–868;
( f ) B. Chen, S. Xiang and G. Qian, Acc. Chem. Res., 2010, 43, 1115–1124.
2 (a) M. Eddaoudi, J. Kim, N. Rosi, D. Vodak, J. Wachter, M. O’Keeffe
and O. M. Yaghi, Science, 2002, 295, 469–472; (b) L. Ma, C. Abney and
W. Lin, Chem. Rev., 2009, 38, 1248–1256; (c) W. Xuan, C. Zhu, Y. Liu
and Y. Cui, Chem. Soc. Rev., 2012, 41, 1677–1695; (d) M. C. Das,
S. Xiang, Z. Zhang and B. Chen, Angew. Chem., Int. Ed., 2011, 50,
10510–10520; (e) S. M. Cohen, Chem. Rev., 2011, 112, 970–1000.
3 (a) A. M. Shultz, O. K. Farha, J. T. Hupp and S. T. Nguyen, J. Am. Chem. Soc.,
2009, 131, 4204–4205; (b) S.-H. Cho, B. Ma, S. T. Nguyen, J. T. Hupp and
T. E. Albrecht-Schmitt, Chem. Commun., 2006, 2563–2565; (c) C. Zhu,
G. Yuan, X. Chen, Z. Yang and Y. Cui, J. Am. Chem. Soc., 2012, 134,
8058–8061; (d) D. N. Dybtsev, A. L. Nuzhdin, H. Chun, K. P. Bryliakov,
E. P. Talsi, V. P. Fedin and K. Kim, Angew. Chem., Int. Ed., 2006, 45, 916–920.
4 (a) L. Ma, J. M. Falkowski, C. Abney and W. Lin, Nat. Chem., 2010, 2,
838–846; (b) M. Yoon, R. Srirambalaji and K. Kim, Chem. Rev., 2011,
112, 1196–1231.
5 (a) Y. Liu, W. Xuan and Y. Cui, Adv. Mater., 2010, 22, 4112–4135;
(b) J. Lee, O. K. Farha, J. Roberts, K. A. Scheidt, S. T. Nguyen and
J. T. Hupp, Chem. Soc. Rev., 2009, 38, 1450–1459; (c) C.-D. Wu, A. Hu,
L. Zhang and W. Lin, J. Am. Chem. Soc., 2005, 127, 8940–8941.
˜
6 (a) C. Baleizao and H. Garcia, Chem. Rev., 2006, 106, 3987–4043; (b) F. Song,
The heterogeneity of the MOF catalyst was also examined. The
supernatant obtained from the oxidation of methyl p-tolyl sulfide
after filtration through a regular filter did not afford any addi-
tional oxidation product. To evaluate the stability of the solid
catalysts, we investigated recycled and reused (R)-1 in the sulfoxi-
dation of methyl p-tolyl sulfide. Upon completion of the reaction,
catalyst 1 could be recovered in quantitative yield and used
repeatedly without significantly degrading the catalytic perfor-
mance for the following three runs (conversions B90% and 46,
42, 44 and 43% ee for 1–4 runs, respectively). PXRD showed that
the recycled catalyst retained crystallinity after four runs, although
the structure got distorted. Inductively coupled plasma optical
C. Wang, J. M. Falkowski, L. Ma and W. Lin, J. Am. Chem. Soc., 2010, 132,
15390–15398; (c) J. M. Falkowski, C. Wang, S. Liu and W. Lin, Angew. Chem.,
Int. Ed., 2011, 50, 8674–8678; (d) A. M. Shultz, A. A. Sarjeant, O. K. Farha,
J. T. Hupp and S. T. Nguyen, J. Am. Chem. Soc., 2011, 133, 13252–13255;
(e) A. M. Shultz, O. K. Farha, D. Adhikari, A. A. Sarjeant, J. T. Hupp and
S. T. Nguyen, Inorg. Chem., 2011, 50, 3174–3176; ( f ) G. Li, W. Yu and Y. Cui,
J. Am. Chem. Soc., 2008, 130, 4582–4583; (g) G. Yuan, C. Zhu, W. Xuan and
Y. Cui, Chem.–Eur. J., 2009, 15, 6428–6434.
7 (a) W. Xuan, M. Zhang, Y. Liu, Z. Chen and Y. Cui, J. Am. Chem. Soc.,
2012, 134, 6904–6907; (b) K. Matsumoto, B. Saito and T. Katsuki, Chem.
Commun., 2007, 3619–3627; (c) H. Egami, T. Oguma and T. Katsuki,
J. Am. Chem. Soc., 2010, 132, 5886–5895; (d) H. Glasner and
E. Y. Tshuva, J. Am. Chem. Soc., 2011, 133, 16812–16814; (e) W. Xuan,
C. Ye, M. Zhang, Z. Chen and Y. Cui, Chem. Sci., 2013, 4, 3154–3159.
8 A. Spek, J. Appl. Crystallogr., 2003, 36, 7–13.
9 H. Frost, T. Du¨ren and R. Q. Snurr, J. Phys. Chem. B, 2006, 110, 9565–9570.
emission spectrometry (ICP-OES) analysis of the product solution 10 P. Adao, F. Avecilla, M. Bonchio, M. Carraro, J. C. Pessoa and
I. Correia, Eur. J. Inorg. Chem., 2010, 5568–5578.
11 I. Fernandez and N. Khiar, Chem. Rev., 2003, 103, 3651.
12 (a) Q. Yang, D. Han, H. Yang and C. Li, Chem.–Asian J., 2008, 3,
indicated little loss of the metal ions (B2 ppm for Cd and 6 ppm
for Ti) from the structure, either as molecular species or as
particles too small to be removed by filtration through Celite.
1214–1229; (b) C. Li, Catal. Rev. Sci. Eng., 2004, 46, 419–492.
c
7122 Chem. Commun., 2013, 49, 7120--7122
This journal is The Royal Society of Chemistry 2013