Abstract:In this work, the utilization of lacunary defects of Wells Dawson polyoxometalate (POM) as platforms to isolate single Ni2+ sites at the molecular level for ethylene oligomerization is reported.
“…[54][55][56][57][58] Recently, we observed Ni-substituted Wells-Dawson-type POM (K 8 P 2 W 17 O 61 •Ni 2+ ) supported on SBA-15 (Ni-POM-WD/ SBA-15) was active for ethylene oligomerization without added co-catalyst. 59 Ni-POM-WD/SBA-15 achieved an ethylene consumption rate of 152 mmol g cat −1 h −1 (4.22 × 10 −5 mol g cat −1 s −1 ) at 200 °C and 2 MPa of ethylene partial pressure, which is comparable to reported Ni-based catalysts. 59 For instance, Ni-SiO 2 -Al 2 O 3 exhibited ethylene oligomerization rates of 0.7-2.7 × 10 −5 mol g cat −1 s −1 at 170-230 °C and 1.5-3.5 MPa.…”
Section: Introductionsupporting
confidence: 67%
“…31 P NMR peaks at these locations correspond to successful metalation of the lacunary POM-WD by Ni. [57][58][59]63 From our previous studies, single crystal XRD of Ni-POM-WD crystals indicates that the Ni sites substitute one of the three tungsten atoms in capping regions of a WD POM, eliminating the probability of the Ni sites being outside of the defect position. 59 In addition, Ni loading of unsupported Ni-POM-WD obtained by ICP corresponds to the nominal loading.…”
Section: Catalyst Preparationmentioning
confidence: 99%
“…59 In addition, Ni loading of unsupported Ni-POM-WD obtained by ICP corresponds to the nominal loading. 59 SBA-15 was prepared using the synthesis procedures described elsewhere. 65,66 First, 18 g of Pluronic 123 (Sigma-Aldrich) and 99.5 g of hydrochloric acid (Millipore Sigma, 37%) were fully dissolved in 550 g of deionized water.…”
Section: Catalyst Preparationmentioning
confidence: 99%
“…In addition, Ni-POM-WD/SBA-15 was successfully regenerated after ethylene oligomerization reaction via helium treatment at 300 °C. 59 Moreover, the dispersion of Ni-POM-WD on the support was shown to be critical, as the unsupported Ni-POM-WD showed no catalytic activity for ethylene oligomerization at 200 °C and 2 MPa due to inaccessibility to Ni sites in the unsupported crystals. 59 Here, we report the performance of a Ni-substituted Wells-Dawson POM for propylene dimerization.…”
Section: Introductionmentioning
confidence: 99%
“…59 Moreover, the dispersion of Ni-POM-WD on the support was shown to be critical, as the unsupported Ni-POM-WD showed no catalytic activity for ethylene oligomerization at 200 °C and 2 MPa due to inaccessibility to Ni sites in the unsupported crystals. 59 Here, we report the performance of a Ni-substituted Wells-Dawson POM for propylene dimerization. The catalytic performance, regenerability, and the kinetic parameters of Ni sites on Ni-POM-WD/SBA-15 for propylene dimerization were determined and compared to literature reports.…”
Olefin oligomerization is an essential step in the production of liquid fuels, chemicals, and chemical precursors. Here, we report gas phase propylene oligomerization catalyzed by isolated Ni2+ sites substituted on...
“…[54][55][56][57][58] Recently, we observed Ni-substituted Wells-Dawson-type POM (K 8 P 2 W 17 O 61 •Ni 2+ ) supported on SBA-15 (Ni-POM-WD/ SBA-15) was active for ethylene oligomerization without added co-catalyst. 59 Ni-POM-WD/SBA-15 achieved an ethylene consumption rate of 152 mmol g cat −1 h −1 (4.22 × 10 −5 mol g cat −1 s −1 ) at 200 °C and 2 MPa of ethylene partial pressure, which is comparable to reported Ni-based catalysts. 59 For instance, Ni-SiO 2 -Al 2 O 3 exhibited ethylene oligomerization rates of 0.7-2.7 × 10 −5 mol g cat −1 s −1 at 170-230 °C and 1.5-3.5 MPa.…”
Section: Introductionsupporting
confidence: 67%
“…31 P NMR peaks at these locations correspond to successful metalation of the lacunary POM-WD by Ni. [57][58][59]63 From our previous studies, single crystal XRD of Ni-POM-WD crystals indicates that the Ni sites substitute one of the three tungsten atoms in capping regions of a WD POM, eliminating the probability of the Ni sites being outside of the defect position. 59 In addition, Ni loading of unsupported Ni-POM-WD obtained by ICP corresponds to the nominal loading.…”
Section: Catalyst Preparationmentioning
confidence: 99%
“…59 In addition, Ni loading of unsupported Ni-POM-WD obtained by ICP corresponds to the nominal loading. 59 SBA-15 was prepared using the synthesis procedures described elsewhere. 65,66 First, 18 g of Pluronic 123 (Sigma-Aldrich) and 99.5 g of hydrochloric acid (Millipore Sigma, 37%) were fully dissolved in 550 g of deionized water.…”
Section: Catalyst Preparationmentioning
confidence: 99%
“…In addition, Ni-POM-WD/SBA-15 was successfully regenerated after ethylene oligomerization reaction via helium treatment at 300 °C. 59 Moreover, the dispersion of Ni-POM-WD on the support was shown to be critical, as the unsupported Ni-POM-WD showed no catalytic activity for ethylene oligomerization at 200 °C and 2 MPa due to inaccessibility to Ni sites in the unsupported crystals. 59 Here, we report the performance of a Ni-substituted Wells-Dawson POM for propylene dimerization.…”
Section: Introductionmentioning
confidence: 99%
“…59 Moreover, the dispersion of Ni-POM-WD on the support was shown to be critical, as the unsupported Ni-POM-WD showed no catalytic activity for ethylene oligomerization at 200 °C and 2 MPa due to inaccessibility to Ni sites in the unsupported crystals. 59 Here, we report the performance of a Ni-substituted Wells-Dawson POM for propylene dimerization. The catalytic performance, regenerability, and the kinetic parameters of Ni sites on Ni-POM-WD/SBA-15 for propylene dimerization were determined and compared to literature reports.…”
Olefin oligomerization is an essential step in the production of liquid fuels, chemicals, and chemical precursors. Here, we report gas phase propylene oligomerization catalyzed by isolated Ni2+ sites substituted on...
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