Two ZnII Metal-Organic Frameworks with Coordinatively Unsaturated Metal Sites
STP), 11.4 wt% (65.0 cm3 gÀ1, STP), and 4.8 wt%
(25.4 cm3 gÀ1, STP) at 195 K, 273 K, and 298 K, respectively.
These values are better than those of MOF-5 (6.2 wt%,
273 K; 3.2 wt%, 298 K) and MOF-177 (3.6 wt%, 298 K) at
1 atm.[13] Based on the CO2 adsorption isotherm at 195 K,
the Brunauer–Emmett–Teller surface area of 2 is calculated
to be about 573 m2 gÀ1, a value much smaller than those of
MOF-5 (3320 m2 gÀ1) and MOF-177 (4508 m2 gÀ1).[13] As
demonstrated above, the framework displays preferential
adsorption of H2 and CO2 over N2 at low temperatures. In
addition, desolvated 2 exhibits selective adsorption of CO2
over CH4 at 273 K. In light of the selective adsorption of H2
over N2 as well as CO2 over CH4, 2 may be applied in hy-
drogen enrichment of the H2/N2 exhaust in ammonia synthe-
sis, natural gas purification, and landfill gas separation, re-
spectively.
The principal mechanisms underlying selective gas ad-
sorption in rigid MOFs are based on a size-exclusion effect
and/or adsorbate–adsorbent interactions. According to the
Horvath–Kawazoe (HK) pore distribution plot of desolvat-
ed 2, the pore diameter of the sample is approximately
4.3 ꢂ (Figure S5 in the Supporting Information). This value
is consistent with the single-crystal analysis and slightly
larger than the kinetic diameter of N2 (3.64 ꢂ), H2 (2.89 ꢂ),
CO2 (3.30 ꢂ), and CH4 (3.76 ꢂ). In our case, the preferen-
tial adsorption of H2 over N2 might be due to the size-exclu-
sion effect, whereas the selective sorption of CO2 over N2
and CH4 might be attributed to a combined effect of size
and of host–guest interactions between CO2 molecules of
a significant quadrupole moment (13.4ꢁ10À40 Cm2) and the
coordinatively unsaturated Zn2+ sites on the host frame-
work.
Desolvated 2 was also subjected to vapor sorption of alco-
hols and water. The sorption isotherms of alcohols present
typical type-I curves with apparent hysteresis loops (Fig-
ure 4c). Approximately 6.2 MeOH, 3.9 EtOH, or 1.8 PrOH
molecules can be absorbed per formula unit at 0.95 atm. It
is clear that the adsorption of alcohol molecules is size-de-
pendent. The vapor-loaded sample powders still display the
characteristic PXRD patterns, thus indicating that the
framework remains stable after alcohol adsorption (Fig-
ure S3d in the Supporting Information). The sorption iso-
therms of water vapor show a hysteretic adsorption behav-
ior, with an uptake of 10.66 wt% (133 cm3 gÀ1, STP) at P/
Po =0.95 (Figure 4d). The water uptake increases abruptly
between 0.08 and 0.13 atm, with an uptake of 6.9 and
48.3 cm3 gÀ1, respectively. It is noted that dehydated 2 takes
Scheme 3. Illustration of the exterior and interior catalytic sites in desol-
vated 2.
posed on the external surface of the framework (blue
arrows) and the other is located on the second layers adja-
cent to the external surface (off-white arrows). Single-crystal
structural analysis shows that the mesh size of 2 is 14.0ꢁ
14.0 ꢂ2 (Figure 1e). Therefore, as long as the substrates are
smaller in size than the meshes, they could access both the
exterior and the interior ZnII CUMs. Nevertheless, smaller-
sized substrates could enter the meshes more easily and
have more chances to access the interior ZnII CUMs. As
a result, 2 might display size-selective catalysis. To character-
ize the possible acid-type catalytic behaviors of the coordi-
natively unsaturated Zn-MOF of 2, carbonyl cyanosilylation
in the presence of desolvated 2 was performed. The addition
of CNÀ to a carbonyl compound to form a cyanohydrin is
À
one of the fundamental C C bond formation reactions in or-
ganic chemistry.[8]
Since 2 is insoluble in most organic solvents (e.g., n-
hexane, dichloromethane, tetrahydrofurane, ethyl acetate,
acetonitrile, and ethanol), we used a 1:2 molar ratio of ben-
zaldehyde and cyanotrimethylsilane in n-hexane at room
temperature to explore the heterogeneous catalysis of desol-
vated 2. We found that a loading of 2.5 mol% of desolvated
2 leads to 100% conversion of benzaldehyde after a reaction
time of 13 hours. By contrast, the removal of 2 by filtration
after 2 hours stopped the reaction, resulting in only 7% ad-
ditional conversion upon stirring for another 12 hours (Fig-
ure S6 in the Supporting Information). The leached Zn con-
tent in the filtrate was measured by inductively coupled
plasma–atomic emission spectroscopy (ICP–AES), and only
a trace amount of Zn (0.1%) was found in the filtrate. In
addition, the reaction in the presence of a mixture of
5 mol% H3TCPB and 7.5 mol% ZnACHTNUTRGNEUNG(NO3)2·6H2O only gives
a conversion of benzaldehyde of 8% under similar condi-
tions. These results evidently demonstrate that 2 acts as an
effective heterogeneous catalyst. The solids of 2 can be
easily isolated from the reaction suspension by simple filtra-
tion and can be reused at least four times with only a slight
decrease in the reactivity (Figure 5). Judging from the
PXRD pattern, the framework of 2 is intact after the fourth
run (Figure S3 in the Supporting Information). According to
our results presented here, the activity of 2 is much higher
up 2.1 water molecules per [Zn3ACHTNUTRGNEUNG(TCPB)2] unit between
these two pressures, thereby indicating coordination of the
water molecules to the Zn ions, which matches well with the
single-crystal X-ray structure.
Size-Selective Catalysis
than that of Cu
Cr3O(H2O)2F(BDC)3 (MIL-101), which is so far the most
powerful Lewis acid catalyst of a MOF. A small amount of
3ACHTUNGTNER(NUNG btc)2 (HKUST-1) but lower than that of
As illustrated in Scheme 3, there are two kinds of ZnII
CUMs that could act as catalytically active sites: one is ex-
A
ACHTUNGTRENNUNG
Chem. Asian J. 2012, 7, 2796 – 2804
ꢀ 2012 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim
2801