ꢁ
1
second step (total 81 mL g ) was released at P = 0.4 MPa
which was higher than 0.1 MPa and that of 1. It is desirable for
remarkable change in the gas adsorption properties, which is
relevant for appropriate gas separation condition with low
energy consumption process.
the regeneration of CO from adsorbed phase.
2
The stepwise adsorption behavior was also observed in
The authors would like to acknowledge Dr. Keiko Miura
and Dr. Keiichi Osaka of SPring-8 for performing the powder
X-ray measurement in beam line BL19B2 in SPring-8. This
work was supported by the New Energy and Industrial
Technology Development Organization (NEDO), Japan.
H O adsorption at 298 K. Although 1 represented single
2
gate-opening type adsorption at 2.2 kPa, 2 gave gradual
uptake until P = 2.2 kPa and a second jump was observed.
Both compounds had large hysteresis in desorption curves
which was indicative of stabilization of water molecule
in the pores. The final adsorption amount of CO
2
for 2 was
Notes and references
1
.5 times larger than that of 1 and comparable to the other
2
1
R. T. Yang, Gas Separation by Adsorption Processes, Imperial
College Press, London, 1997.
2–24
adsorbents.
The low flexibility in 2 also affected an
. The 2 provided negligible amount of uptake
isotherm of CH
4
2 S. Kitagawa, R. Kitaura and S. Noro, Angew. Chem., Int. Ed.,
004, 43, 2334–2375.
2
for CH even at pressure of 1.0 MPa at 273 K. Although 1
4
3
D. Britt, D. Tranchemontagne and O. M. Yaghi, Proc. Natl. Acad.
Sci. U. S. A., 2008, 105, 11623–11627.
4 V. Finsy, H. Verelst, L. Alaerts, D. De Vos, P. A. Jacobs,
ꢁ
1
,
gradually adsorbed CH4 until P = 0.65 MPa (10 mLg
ꢁ1
Fig. 1c) and showed abrupt uptake to reach 58 mL g at
ꢁ
1
G. V. Baron and J. F. M. Denayer, J. Am. Chem. Soc., 2008,
130, 7110–7118.
J. R. Li, R. J. Kuppler and H. C. Zhou, Chem. Soc. Rev., 2009, 38,
0
.95 MPa, 2 adsorbed only 4 mL g at 1.0 MPa, resulting in
the better selectivity on CH /CO . The low flexiblity of 2 for
is unique for creation of repulsive property against the
molecule at wide pressure range. It provides another idea
/CO separation with other metal–
organic frameworks having rigid porous scaffold and preferable
4
2
5
CH
CH
4
4
1477–1504.
6 S. Q. Ma and H. C. Zhou, Chem. Commun., 2010, 46, 44–53.
7
B. Chen, S. Xian and G. Qian, Acc. Chem. Res., 2010, 43,
115–1124.
L. Bastin, P. S. Barcia, E. J. Hurtado, J. A. C. Silva,
of PCPs/MOFs for CH
4
2
1
8
2
5–27
binding character for CO
We checked the separation ability of CO
from CH /CO mixture gas and executed the co-adsorption
2
gas.
A. E. Rodrigues and B. Chen, J. Phys. Chem. C, 2008, 112,
1
575–1581.
L. Hamon, P. L. Llewellyn, T. Devic, A. Ghoufi, G. Clet,
V. Guillerm, G. D. Pirngruber, G. Maurin, C. Serre, G. Driver,
2
over CH
4
9
4
2
measurement by use of our hand-made instrument. We dosed
W. van Beek, E. Jolimaitre, A. Vimont, M. Daturi and G. Fe
J. Am. Chem. Soc., 2009, 131, 17490–17499.
0 G. Ferey and C. Serre, Chem. Soc. Rev., 2009, 38, 1380–1399.
1 S. Horike, S. Shimomura and S. Kitagawa, Nat. Chem., 2009, 1,
95–704.
12 H. S. Choi and M. P. Suh, Angew. Chem., Int. Ed., 2009, 48,
865–6869.
3 P. C. LeBaron, Z. Wang and T. J. Pinnavaia, Appl. Clay Sci., 1999,
5, 11–29.
4 S. R. J. Oliver, Chem. Soc. Rev., 2009, 38, 1868–1881.
´
rey,
mixture gas (CH : CO = 1 : 1(vol)) for 2 under the condition
4
2
1
1
´
of total pressure 0.1 MPa and 273 K then waited three hours
for the equilibrium co-adsorption process and detected the
adsorbed gas species by gas chromatography. Although the
6
ꢁ
1
6
total adsorbed amount of gas was low (17 mL g ) because of
the low total pressure in this measurement, we hardly observed
1
1
1
the trace of CH
4
which indicated that all the adsorbed gas was
from
CO , and we observed clear separation property for CO
2
2
15 A. Kondo, H. Noguchi, L. Carlucci, D. M. Proserpio, G. Ciani,
H. Kajiro, T. Ohba, H. Kanoh and K. Kaneko, J. Am. Chem. Soc.,
mixture gas. The adsorption is corresponding to the first
2
007, 129, 12362–12363.
uptake of CO for 2 in Fig. 2c. Taking the single adsorption
2
1
6 S. Horike, D. Tanaka, K. Nakagawa and S. Kitagawa, Chem.
Commun., 2007, 3395–3397.
isotherms of CO and CH into consideration, the compound
2
4
2
is expected to show high separation ability in a wide
17 R. Kitaura, K. Seki, G. Akiyama and S. Kitagawa, Angew. Chem.,
Int. Ed., 2003, 42, 428–431.
range of pressure, especially above 0.1 MPa. Evaluation of
separation performance from mixture gas at higher pressure
and temperature is under investigation.
1
8 J. Seo, H. Sakamoto, R. Matsuda and S. Kitagawa, J. Nanosci.
Nanotechnol., 2010, 10, 3–20.
19 A. L. Spek, J. Appl. Crystallogr., 2003, 36, 7–13.
2
0 J. Y. Lee, D. H. Olson, L. Pan, T. J. Emge and J. Li, Adv. Funct.
Mater., 2007, 17, 1255–1262.
Based on the crystallographic information of 1, we enlarged
the size of the flexible ligand for tuning of activation energy of
structural transformation and gave suitable flexibility for
2
1 R. Buchecker, T. Lukac and C. Benecke, U.S. Patent,
WO 00/48985, 2000.
22 J. W. Yoon, S. H. Jhung, Y. K. Hwang, S. M. Humphrey,
CH /CO
4
2
separation at the total pressure of zero to 1.0 MPa.
above 0.1 MPa and it allows gas
P. T. Wood and J. S. Chang, Adv. Mater., 2007, 19, 1830–1834.
3 C. A. Grande and A. E. Rodrigues, Ind. Eng. Chem. Anal. Ed.,
007, 46, 4595–4605.
2
releases adsorbed CO
2
2
recovery without vacuum. The flexibility herein is the
combination of a layer–layer interaction and local flexibility
of coordination bonds in the layer and the approach is feasible
only if we employ the 2D porous coordination layer.
2
24 S. G. Li, J. L. Falconer and R. D. Noble, Microporous Mesoporous
Mater., 2008, 110, 310–317.
2
5 Y. S. Bae, O. K. Farha, A. M. Spokoyny, C. A. Mirkin, J. T. Hupp
and R. Q. Snurr, Chem. Commun., 2008, 4135–4137.
6 B. Mu, F. Li and K. S. Walton, Chem. Commun., 2009, 2493–2495.
In conclusion, we demonstrated that the minor modification
of the ligand moiety in the layer framework causes a
2
27 Y. M. Shen and J. F. Bai, Chem. Commun., 2010, 46, 1308–1310.
This journal is c The Royal Society of Chemistry 2010
Chem. Commun., 2010, 46, 9229–9231 9231