2202
F.-N. Shi et al. / Journal of Solid State Chemistry 184 (2011) 2196–2203
Fig. 9. Cyclopropanation of styrene with ethyldiazoacetate.
(more yellowish), the PXRD pattern of the former (Fig. 8) shows
the presence of (1).
Table 4
Results of the cyclopropanation of styrene with EDA using the Cu(I) MOF as
catalyst.a
f
Run t (h) %Cub %Cc %transc,d
TONe TOF (hꢁ1
)
4. Conclusions
F
C
This work reports the synthesis, structure and catalytic activity of
a new ‘hybrid’ MOF with mixed organic and inorganic linkers, in the
Cu(I) MOFg
Cu(I) MOFh
1st
24
48
0.9
0.9
20
23
19
18
20
9
51
55
62
54
58
46
57
52
57
72
72
73
66
73
67
60
66
71
23
27
22
21
0.97
0.56
0.92
0.19
2nd
3th
4th
1st
copper-(4,40-bpy)-sulfate system. With a suitable reductant,
L-aspar-
24
tic acid, we have successfully prepared a Cu(I) supramolecular MOF,
110
28
[Cu2(SO4)(4,40-bipy)2]4 ꢀ 24H2O, under mild hydrothermal condi-
3
˚
2nd
96
tions. The volume (10106.1 A ) of the unit cell of (1) is relatively
No catalyst
CuSO4þ4,40-bpy
CuBox
24
7
considerable, much larger than the volume of a similar structure
110
3
0.9
1.0
7
3
˚
previously reported [16] (2519.34 A ) although both materials have
93
95
32
the same secondary building unit. The structure of (1) consists of
Cu(I) nodes linked by 4,40-bpy into infinite chains, and sulfate
groups connecting two neighboring chains, resulting in a 1-D double
chain network. Guest water molecules establish a complicated
network of hydrogen bonding interactions with their neighboring
oxygen and sulfur atoms, leading to the formation a 3-D supramo-
lecular framework. (1) was tested as a heterogeneous catalyst in the
cyclopropanation of styrene showing a high trans cyclopropane
diastereoselectivity and could be recycled and reused for three
consecutive cycles without significant loss of catalytic activity.
a
Reactions performed at room temperature using 5.00 mmol styrene,
1.80 mmol n-undecane (internal standard), 139 mg of MOF and 5.50 mmol of
EDA in 10.0 ml of CH2Cl2.
b
Cu molar% relatively to styrene.
c
Determined by CG-FID.
d
%trans ¼trans ꢂ 100/(transþcis); F¼diethyl fumarate, trans by-product from
the dimerization of EDA (cis¼diethyl maleate); C¼cyclopropane.
e
TON¼moles of styrene converted/moles of Cu.
f
TOF¼TON/time of reaction.
g
Reaction performed without constant stirring.
h
Reaction performed under constant magnetic stirring at 1000 rpm.
a slightly higher trans cyclopropane diastereoselectivity (73%).
In the next cycle the reaction slowed down and comparable
styrene conversion was achieved only after 110 h with decrease
in the trans cyclopropane diastereoselectivity (66%).
It is noteworthy that the reaction was also performed under
constant stirring conditions with similar catalytic performance as
without stirring but in the second cycle the activity was much
lower than without stirring, which may be due to the difficult
recycling of the crushed MOF crystals.
Acknowledgments
~
ˆ
We acknowledge Fundac-ao para a Ciencia e a Tecnologia (FCT) for
funding (PTDC/QUI/ 65805/2006, FCOMP-01–0124-FEDER-007424)
and Fundo Social Europeu. F.-N. SHI and A.R. Silva acknowledge FCT
ˆ
for Ciencia 2007 and 2008 programs, respectively.
Appendix A. Supplementary material
In the control experiment using comparable amounts of
copper(II) sulfate (0.9% mol) and 4,40-bpy (0.9% mol) as those
contained in MOF (1) catalytic reactions styrene conversion after
110 h was similar to the control experiment where no catalyst
was used. Hence, the catalytic reactions with (1) were truly
heterogeneous and any copper leaching into the solution was
not responsible for the observed MOF (1) activity in the cyclo-
propanation reaction.
It is worth to mention that three copper(I) complexes with
2,20-bipyridine and styrene were already reported to be homo-
geneous catalysts in the cyclopropanation of styrene [43]. Cyclo-
propane diastereoselectivities of 68.2, 69.9 and 82.0, depending
on the counterion coordinated and complex structure, can be
calculated from the results presented in this paper using a
different product analysis methodology. Therefore the present
copper(I) MOF is more diastereoselective than most of these
reported homogeneous copper(I) complexes.
Supplementary material associated with this article can be
References
[1] A.J. Fletcher, K.M Thomas, M.J. Rosseinsky, J. Solid State Chem. 178 (2005)
2491–2510.
´
[2] D.J. Tranchemontagne, J.L. Mendoza-Cortes, M. O’Keeffe, O.M. Yaghi, Chem.
Soc. Rev. 38 (2009) 1257–1283.
[3] O.K Farha, J.T. Hupp, Acc. Chem. Res. 43 (2010) 1166–1175.
[4] J.-P. Zhang, X.-C. Huang, C.-X. Ming, Chem. Soc. Rev. 38 (2009) 2385–2396.
[5] S Natarajan, P. Mahata, Chem. Soc. Rev. 38 (2009) 2304–2318.
[6] H.Y. Yang, L.K. Li, J. Wu, H.W. Hou, B. Xiao, Y.T. Fan, Chem. -Eur. J. 15 (2009)
4049–4056.
[7] J.-R. Li, D.J Timmons, H.-C. Zhou, J. Am. Chem. Soc. 131 (2009) 6368–6369.
[8] Y.-G. Huang, F.-L. Jiang, M.-C. Hong, Coordin. Chem. Rev. 253 (2009)
2814–2834.
[9] X. Gan, W.-F. Fu, Y.-Y. Lin, M. Yuan, C.-M. Che, S.-M. Chi, H.-F. Jie, Li, J.-H. Chen,
Y. Chen, Z.-Y. Zhou, Polyhedron 27 (2008) 2202–2208.
[10] A. Almesa˚ ker, S.A. Bourne, G. Ramon, J.L. Scott, C.R. Strauss, Cryst. Eng.
Commun. 9 (2007) 997–1010.
[11] A.G. Bingham, H. Bo¨gge, A. Mu¨ller, E.W. Ainscough, A.M. Brodie, J. Chem. Soc.,
Dalton Trans. (1987) 493–499.
[12] S.P. Foxon, G.R. Torres, O. Walter, J.Z. Pedersen, H. Toftlund, M. Hu¨ber, K. Falk,
W. Haase, J. Cano, F. Lloret, M. Julve, S. Schindler, Eur. J. Inorg.Chem. (2004)
335–343.
Clearly, MOF (1) is a heterogeneous catalyst with moderate
activity in the cyclopropanation of styrene, high trans diastereos-
electivity, and it may be recycled and reused at least for three
consecutive catalytic cycles with a total turnover number (TON)
of 93, similar to the best homogeneous catalyst reported for this
reaction (CuBox, Table 4). Although the color of the recycled
catalyst is more greenish than the color of the parent material