“…33 On the contrary, there is a typical peak of metal Pd at 40.3°in the XRD pattern of Pd1.6/rGO (Figure S1d), which may be because the Pd NPs disperse worse on rGO than CN-rGO. 37 The CO pulse chemisorption results prove the above conclusion, the Pd dispersion of Pd@CN-rGO is as high as 24%, more than 6 times that of Pd1.6/rGO (Table 2), and the rGO content has no significant influence on the Pd dispersion. The higher Pd dispersion of Pd@CN-rGO should be caused by the ZIF-derived CN.…”
Selective hydrogenation of phenol is a green strategy to produce cyclohexanone. Achieving high phenol conversion and cyclohexanone selectivity under mild conditions is a significant challenge in the design and synthesis of highly efficient catalysts. Herein, a highly efficient Pd@CN-rGO catalyst is synthesized by supporting Pd nanoparticles on the composite of ZIF-derived N-doped carbon and reduced GO (CN-rGO), which is prepared via annealing the composite of layered ZIF-L-Co and GO.
“…33 On the contrary, there is a typical peak of metal Pd at 40.3°in the XRD pattern of Pd1.6/rGO (Figure S1d), which may be because the Pd NPs disperse worse on rGO than CN-rGO. 37 The CO pulse chemisorption results prove the above conclusion, the Pd dispersion of Pd@CN-rGO is as high as 24%, more than 6 times that of Pd1.6/rGO (Table 2), and the rGO content has no significant influence on the Pd dispersion. The higher Pd dispersion of Pd@CN-rGO should be caused by the ZIF-derived CN.…”
Selective hydrogenation of phenol is a green strategy to produce cyclohexanone. Achieving high phenol conversion and cyclohexanone selectivity under mild conditions is a significant challenge in the design and synthesis of highly efficient catalysts. Herein, a highly efficient Pd@CN-rGO catalyst is synthesized by supporting Pd nanoparticles on the composite of ZIF-derived N-doped carbon and reduced GO (CN-rGO), which is prepared via annealing the composite of layered ZIF-L-Co and GO.
“…While no obvious Pd peaks are observed in the other catalysts. This difference may be due to the high Pd content of the catalysts prepared with alcohol solvents as discussed below, and the weak reducibility of alcohol solvents to Pd. , The Fourier transform infrared (FT-IR) spectra of six typical catalysts, that is, Pd@PC-COF-Pen, Pd@PC-COF-PE, Pd@PC-COF-NBA, Pd@PC-COF-EA, Pd@PC-COF-Dio, and Pd@PC-COF-MeOH, are shown in Figure B. Compared with the FT-IR spectrum of PC-COFs, the FT-IR spectra of Pd@PC-COFs do not change significantly, indicating that the introduction of active component Pd using wet impregnation with different solvents does not obviously vary the groups of the PC-COFs.…”
Selective
phenol hydrogenation is a valuable route to produce cyclohexanone,
but it poses a great challenge. Herein, a series of Pd@PC-COFs catalysts
were prepared by the wet impregnation with different solvents. The
impregnation solvent has a great influence on the microstructures
and surface characteristics of the Pd@PC-COFs catalysts and their
catalytic properties in the selective phenol hydrogenation to cyclohexanone.
The as-prepared Pd@PC-COF-NBA catalyst shows the highest catalytic
activity, with a phenol conversion of 98.3% at the cyclohexanone selectivity
of 98.9%, which is 5.3 times that of Pd@PC-COF-MeOH and 2.4 times
that of Pd@PC-COF-DI. Larger specific surface area, well-developed
pore structures, rich mesoporous ratio, higher Pd content and Pd(0)
ratio, and improved Pd dispersion are the important reasons for the
superior catalytic performance of Pd@PC-COF-NBA. Pd@PC-COF-EA and
Pd@PC-COF-Dio exhibit good catalytic stability during five reaction
cycles. These findings can aid the development of high-performance
Pd@COFs for the selective phenol hydrogenation.
“…Table 1 Figure 2 shows the XRD patterns of the three reduced catalysts, where it can be clearly observed the presence of two broad peaks centered at around 26. These peaks associated to metallic Pd are not observed in the XRD pattern of AgPdCl/C catalyst, suggesting a high dispersion and consequently a lower palladium crystal sizes due to the utilization of PdCl2 precursor in the synthesis of this catalyst [46].…”
Section: Figurementioning
confidence: 92%
“…It is worth to mention that AgPdN/C catalyst yielded the lowest ABET and Vmicro values, probably due to larger metal particles associated to the use of nitrate as Pd precursor. It has been reported that PdCl2 leads to metal particles with higher dispersion than Pd(NO3)2, due to the stronger interaction of this last with the activated carbon surface [46,47].…”
Section: Characterization Of the Catalystsmentioning
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