| Literature DB >> 30693174 |
Lin-Qiang Mo1, Xian-Fei Huang2, Guan Huang1, Guang-Ping Yuan1, Su-Juan Wei1.
Abstract
We aimed at elevating catalytic performances of cobalt tetrakis(pentafluorophenyl)porphyrin (Entities:
Keywords: catalysis; cobalt porphyrin; covalently grafting-action and axial coordination; nanocavity; promotion
Year: 2019 PMID: 30693174 PMCID: PMC6345221 DOI: 10.1002/open.201800268
Source DB: PubMed Journal: ChemistryOpen ISSN: 2191-1363 Impact factor: 2.911
Figure 1SEM and STEM images of np‐CTS, nonp‐CTS, Co TPFPP/np‐CTS, and Co TPFPP/nonp‐CTS; EDS images of Co TPFPP/np‐CTS (a), Co TPFPP/nonp‐CTS (b), and Co TPFPP/np‐CTS recovered after 5th run of recycle (c),inserts are the EDS elemental mapping of Co, N, C, O, and F.
Scheme 1Synthetic route for the preparation of Co TPFPP/np‐ or nonp‐CTS.
Figure 2The N2 adsorption/desorption isotherm and BJH pore‐size distribution curves of np‐CTS (left) and Co TPFPP/np‐CTS (right).
Physical properties of np (nonp)‐CTS and Co TPFPP/np (nonp)‐CTS.
| Materials | Surface area [m2 g−1] | Pore diameter [nm] |
|---|---|---|
| np‐CTS | 89.5 | 20.6 |
| Co TPFPP/np‐CTS | 77.2 | 17.7 |
| nonp‐CTS | 2.5 | – |
| Co TPFPP/nonp‐CTS | 2.1 | – |
Figure 3UV/Vis spectra for the DCM solutions of Co TPFPP (ϵ=3.40×105 L ⋅ mol−1 ⋅ cm−1), and for DCM suspensions of Co TPFPP/np‐CTS (ϵ=8.27×103 mol−1 ⋅ cm−1), Co TPFPP/nonp‐CTS(ϵ=8.28×103 mol−1 ⋅ cm−1).
Figure 4FTIR spectra for np(or nonp)‐CTS and Co TPFPP/np(or nonp)‐CTS with an effective frequency range of 800–400 cm−1 (top), FTIR spectra for CTS, np‐CTS, Co TPFPP, Co TPFPP/np‐CTS, np‐CTS + Co TPFPP (left), and CTS, nonp‐CTS, Co TPFPP, Co TPFPP/nonp‐CTS, nonp‐CTS + Co TPFPP (right) with an effective frequency range of 4000–400 cm−1.
Figure 5Resonance Raman spectra of np‐CTS, Co TPFPP, Co TPFPP/np‐CTS (left), and nonp‐CTS, Co TPFPP, Co TPFPP/nonp‐CTS (right), pulsed excitation at 325 nm.
The binding energy of the key elements in CoTPFPP/np (nonp‐)‐CTS, Co TPFPP, and np (nonp‐)‐CTS.
| XPS spectra | Existing form ofthe key elements | Binding Energy [eV] | |||
|---|---|---|---|---|---|
| Co TPFPP/np‐CTS (Co TPFPP/nonp‐CTS) | Co TPFPP | np‐CTS (nonp‐CTS) | dBE [eV] | ||
| Co2p |
| 804.5(803.9) | 795.9 | – | 8.6(8.0) |
| 784.2(784.2) | 780.6 | – | 3.6(3.6) | ||
| N 1s |
| 399.6(399.2) | 399.1 | – | 0.5(0.1) |
|
| 399.4(399.0) | 399.0 | – | 0.4(0.0) | |
|
| 399.2(398.6) | – | 398.1(399.6) | 1.1(‐1.0) | |
|
| 401.9(401.2) | – | 400.9(400.1) | 1.0(1.1) | |
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| 402.5(402.7) | – | 402.5(402.8) | 0.0(‐0.1) | |
| C1s | C= | 284.8(285.4) | 287.9 | — | |
| C= | 284.7(284.6) | – | ‐3.2(‐3.3) | ||
Figure 6X‐ray photoelectron spectra and main spectral bands based on the BE of the Co, N, and C elements for np‐CTS, Co TPFPP, Co TPFPP/np‐CTS (top), and nonp‐CTS, Co TPFPP,and Co TPFPP/nonp‐CTS (bottom).
Figure 7Changes in the TOF (left) and TON (right) of the catalysts with reaction time, under cyclohexane oxidation reaction conditions optimized by RSM. Reaction conditions: O2 flow rate= 0.03 m3.h−1 and 3.5 hours reaction time.
Comparison of catalytic performances of related catalysts under the best RSM‐optimized reaction conditions.[a]
| Catalyst | Run | TOF (×105 h−1) | TON (×105) | Yield [%] | Selectivity [%] |
|---|---|---|---|---|---|
| Co TPFPP/np‐CTS | 1 | 2.5 | 8.7 | 26.4 | 65.0 |
| 2 | 3.7 | 12.9 | 25.9 | 64.1 | |
| 3 | 6.6 | 23.1 | 25.2 | 62.9 | |
| 4 | 9.3 | 32.4 | 23.0 | 61.5 | |
| 5[b] | 10.4 | 36.5 | 20.7 | 60.3 | |
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| Co TPFPP | 1 | 1.6 | 5.6 | 18.5 | 72.0 |
| Co TPFPP+CTS | 1 | 1.6 | 5.7 | 18.7 | 70.4 |
| Co TPFPP/nonp‐CTS | 1 | 1.3 | 4.4 | 13.9 | 69.9 |
| 2 | 1.7 | 6.0 | 13.4 | 69.3 | |
| 3 | 2.4 | 8.3 | 11.6 | 69.1 | |
| 4 | 3.6 | 12.5 | 11.0 | 68.4 | |
| 5 | 4.9 | 17.2 | 10.7 | 68.0 | |
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[a] 200 mLcyclohexane, 165.14 °C, 0.8 MPa, 0.98 mg Co TPFPP, oxygen flow rate of 0.03 m3/h, and reaction time of 3.5 hours. TOF: turnover frequency; TON: turnover number. [b] Its reuse was not stopped here.
Figure 8Top) The TOF (left) and TON (right) of cyclohexane oxidation over various catalysts reused. Bottom) the total TOF (left) and TON (right) of cyclohexane oxidation over different catalysts.