Crystal Growth & Design
Article
g−1, respectively. The BET surface area of 1a is slightly smaller
than those microporpous porphyrin-based MOFs with the 2D
layered configurations.57,58 There is adsorption−desorption
hysteresis on the N2 sorption curve, indicating the existence of
micropores in 1a. The experimental pore size distribution
median pore width is 0.99 nm and maximum pore volume is
0.052 cm3·g−1.
ASSOCIATED CONTENT
* Supporting Information
Refer to CCDC 1411460 for crystallographic data in CIF
format. The Supporting Information is available free of charge
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S
TGA, N2 sorption isotherms, crystallographic data
The CO2 sorption properties on desolvated 1a at two
different temperatures (273 and 298 K) were also evaluated. As
shown in Figure 4a, the CO2 adsorption isotherms of 1a at both
273 and 298 K are nonclassical type I adsorption isotherms and
the CO2 uptakes are 42.18 cm3·g−1 (8.28 wt %) and 30.19 cm3·
g−1 (5.93 wt %) at 273 and 298 K, respectively. It is obvious
that the final CO2 uptake values of 1a at both 273 and 298 K
are higher than reported porphyrin based HOF,49 which is
comparable to some previously reported MOFs.59 All sorption
isotherms of 1a at 273 and 298 K show hysteresis. In order to
further study gas sorption behaviors of 1a, the adsorption
enthalpy of the HOF 1a to CO2 molecules (Figure 4b) was
calculated according to the CO2 gas adsorption isotherms at
273 and 298 K, utilizing a built-in function in Micromeritics
ASAP 2020 analyzer based on the Virial equation (shown in the
adsorption for 1a at zero coverage is 23.20 KJ·mol−1, which is
comparable to those found in MOFs with small pores.60
3.4. Catalytic Activity of 1. We examined 1 for its catalytic
oxidation to ethylbenzene. The ethylbenzene oxidation was
performed in solvent of acetonitriler at 80 °C using tert-
butylhydroperoxide (TBHP) as the oxidant, with GC
monitored throughout the reaction. The results (Table 1)
show that 1 efficiently catalyzes the conversion of ethylbenzene
to the only product acetophenone quantitatively in 83.1% yield.
After reaction finished, solid 1 was easily recovered by
tion) and subsequently used in successive runs with only
slightly decreased product yields. The conversion after six
cycles is 72.7%. When the substrate was changed to 1-
phenylpropane, 1,2,3,4-tetrahydronaphthalene, and diphenyl-
methane, the conversion was decreased to 35.8%, 75.1%, and
24.8%, respectively. There is no obvious change in the P-XRD
pattern (Figure 3) except that peaks at 2θ = 19° and 2θ = 21°
disappeared in the curve of recovered 1, indicating that the
framework and pore are kept after the reaction.
AUTHOR INFORMATION
Corresponding Author
Notes
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The authors declare no competing financial interest.
ACKNOWLEDGMENTS
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This work has been supported by the NNSF (No. 21271148).
We are very grateful to Shaanxi Normal University for their
kind assistance.
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