Bing Liu,
Suyun Jie*,
Zhiyang Bu and
Bo-Geng Li
State Key Laboratory of Chemical Engineering, College of Chemical and Biological Engineering, Zhejiang University, Hangzhou 310027, China. E-mail: jiesy@zju.edu.cn; Fax: +86 57187951612; Tel: +86 57187951515
First published on 13th November 2014
A series of mixed-linker metal–organic frameworks (Zn4O(BDC)x(ABDC)3−x) has been synthesized, and then transformed into nickel catalysts for ethylene oligomerization through quantitative postsynthetic modification. These complexes were more manageable, more stable, and more economic than analogues of IRMOF-3 (x = 0) by post-modification.
The synthesis of MixMOFs (MixMOF-a, MixMOF-b, MixMOF-c) was performed by using a similar procedure for IRMOF-3, expect that partial 2-aminobenzene-1,4-dicarboxylate (H2ABDC) linkers were substituted by 1,4-benzenedicarboxylate (H2BDC).15–17 Zn(NO3)2·6H2O was dissolved in DMF and then the proportional H2ABDC and H2BDC were added to the solution. After the mixture was heated at 100 °C for 48 h, the cubic-shape crystals formed were washed with DMF and then soaked in CHCl3. The purity and structural integrity of synthesized MixMOFs were confirmed by powder X-ray diffraction (PXRD), TG and BET analyses. Since the single-crystal data of IRMOF-1 (x = 0) and IRMOF-3 (x = 3) are very similar,18 it seems to be obvious that the powder patterns of all the MixMOFs should be more or less identical. Undoubtedly, IRMOF-3 gives the minimum BET surface area because of more amino groups. To determine the x value in the MixMOFs (Zn4O(ABDC)x(BDC)3−x), these crystals were digested in DCl/D2O and [D6]DMSO and then analyzed by 1H NMR spectroscopy (Fig. 1).16,19,20 There is a slightly lower incorporation of amino groups into the MixMOFs than that in the feed (Table 1), which is consistent with the reported results for other mixed-ligand MOFs.21,22
MOFs | Feed ratio of H2ABDC/H2BDC | ABDC/BDC in MixMOFsa | NH2 contenta (10−4 mol g−1) | Postsynthetic complexes | Time (d) | Ni contentb (10−3 mol g−1) | Ni contentc (10−3 mol g−1) |
---|---|---|---|---|---|---|---|
a Determined by 1H NMR.b Theoretical value.c Measured by ICP. | |||||||
MixMOFs-a | 1/5 | 1.85/10.15 | 5.95 | MixMOFs-a-Ni | 1 | 0.50 | 0.65 |
MixMOFs-b | 1/3 | 2.53/9.47 | 8.12 | MixMOFs-b-Ni | 2 | 0.65 | 1.07 |
MixMOFs-c | 1/2 | 3.43/8.57 | 10.95 | MixMOFs-c-Ni | 3 | 0.82 | 1.22 |
IRMOF-3 | 1/0 | — | 36.81 | IRMOF-3-Ni-a | 1 | — | 0.17 |
IRMOF-3 | 1/0 | — | 36.81 | IRMOF-3-Ni-b | 2 | — | 0.20 |
IRMOF-3 | 1/0 | — | 36.81 | IRMOF-3-Ni-c | 3 | — | 0.14 |
IRMOF-3 | 1/0 | — | 36.81 | IRMOF-3-Ni-d | 4 | — | 0.18 |
After dried at 100 °C under vacuum for 12 h, all the above MOFs were treated with green solutions containing 2-pyridine carboxaldehyde (PyCHO) and NiBr2 in methanol at room temperature (Table 1).23 The imine condensation reaction occurred in the presence of excess of Ni(PyCHO)Br2 to directly generate the imino-pyridine nickel complexes anchored into MOFs (Scheme 1). During the reaction, the color of solids slowly changed from light orange to yellowish green for MixMOFs (orange to yellowish green for IRMOF-3). In the FT-IR spectra, apparent amino can be observed for IRMOF-3-Ni, even if the reaction time was prolonged to 4 days (Fig. S1†); however, no residual characteristic peaks of amino were found for MixMOFs-Ni after modification (Fig. S2–4†), indicating all the amino groups in MixMOFs have been transformed into imino groups. From this perspective, the reactive groups in MixMOFs can achieve an entire utilization without any waste by using this mixed-linker method.
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Scheme 1 The quantitatively postsynthetic modification of MixMOFs to yield MOFs-containing Ni catalysts. |
ICP proved that IRMOF-3 had a limitation of postsynthetic modification and any reinforce in the concentration of starting material and the reaction time would not increase the content of nickel. Whereas, the content of nickel increased along with amino contents in MixMOFs, so the density of active sites could be customized. In other word, the amount of active sites introduced by postsynthetic modification can be controlled by adjusting the ratio of H2ABDC and H2BDC during the synthesis of MOFs. As IRMOF-1 exists inevitable ion exchange,24–26 the actual measured values are larger than theoretical calculated ones (Table 1).
Externally, all the MOFs showed no signs of degradation and maintained their block-like appearance after post-modification. PXRD and N2 adsorption isotherms methods were carried out to confirm the structural integrity and porosity of the modified MOFs. The nickel catalysts containing MixMOFs retained the structural integrity after modification, showing similar peak positions and intensities (Fig. 2a, S5 and S6†). As expected, the post-modification is accompanied by a reasonable decrease of the BET surface (Fig. S10–12 and Table S1†). With regard to IRMOF-3, its crystallinity was destroyed very much even with the reaction time of one day and the surface area decayed to single-digit level (Fig. 2b, S7, S11 and Table S1†). Therefore, the mix-linker method can also improve the MOFs stability for post-modification. In addition, TGA analysis indicated that the nickel catalysts containing MixMOFs had better thermal stability than IRMOF-3-Ni (Fig. S8 and S9†).
Given the fact that an analogue was very efficient in the selective dimerization of ethylene,23 the catalytic activity of above nickel catalysts containing MOFs was evaluated in the oligomerization of ethylene in toluene in the presence of Et2AlCl (Table 2).
Entry | Cat. | Activity (104 g mol−1 h−1) | Selectivityb (%) | ||
---|---|---|---|---|---|
C4 | C6 | C8+ | |||
a Reaction conditions: 30 μmol of Ni, Et2AlCl![]() ![]() |
|||||
1 | MOFsc | 0 | 0 | 0 | 0 |
2 | MOFs + PyCHOd | 0 | 0 | 0 | 0 |
3 | MOFs + NiBr2e | 0 | 0 | 0 | 0 |
4 | MixMOFs-Ni-a | 5.82 | 71.3 | 6.9 | 21.8 |
5 | MixMOFs-Ni-b | 6.91 | 79.5 | 7.2 | 13.2 |
6 | MixMOFs-Ni-c | 5.60 | 79.5 | 6.2 | 14.3 |
7 | IRMOF-3-Ni-a | 6.29 | 35.0 | 9.3 | 55.7 |
8 | IRMOF-3-Ni-d | 5.28 | 39.6 | 8.2 | 52.2 |
9 | MixMOFs-Ni-bf | 5.41 | 82.7 | 2.7 | 14.6 |
10 | MixMOFs-Ni-bg | 13.1 | 92.4 | 2.6 | 5.0 |
11 | MixMOFs-Ni-bh | 46.0 | 92.7 | 6.1 | 1.2 |
12 | MixMOFs-Ni-bi | 18.4 | 92.3 | 3.7 | 4.0 |
In view of the fact that all three MOFs alone or their mixture with either PyCHO or NiBr2 didn't show any activity (entries 1–3 in Table 2), it is noteworthy that all the catalysts exhibited comparative activities and gave different selectivity. For IRMOF-3-Ni, its crystallinity has been severely damaged, and the residual amino may affect the reaction process as a Lewis base, giving a worse selectivity for ethylene dimerization (entries 7 and 8 in Table 2). Instead, the MixMOFs-Ni catalysts retained their structural integrity so that the active Ni centers were thought to be anchored into MOFs,27,28 and the corresponding reactions should occur in the hole of MOFs, producing better selectivity for ethylene dimerization. MixMOFs-Ni-a with maximum specific surface area produced more long-chain olefins, and MixMOFs-Ni-b gave the highest activity with appropriate density of active centers. In addition, for this heterogeneous system, reaction conditions would determine the ethylene concentration near the active centers, so that the activity and the selectivity for ethylene dimerization were largely influenced by reaction temperature, ethylene pressure and amount of cocatalyst (entries 5 and 9–12 in Table 2).
Footnote |
† Electronic supplementary information (ESI) available: Experimental procedures, Fig. S1–S12 and Table S1. See DOI: 10.1039/c4ra10605a |
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